US12420221B2 - Multi-layered electret-containing filtration media - Google Patents
Multi-layered electret-containing filtration mediaInfo
- Publication number
- US12420221B2 US12420221B2 US15/217,718 US201615217718A US12420221B2 US 12420221 B2 US12420221 B2 US 12420221B2 US 201615217718 A US201615217718 A US 201615217718A US 12420221 B2 US12420221 B2 US 12420221B2
- Authority
- US
- United States
- Prior art keywords
- equal
- layer
- less
- filter media
- fibers
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D39/00—Filtering material for liquid or gaseous fluids
- B01D39/14—Other self-supporting filtering material ; Other filtering material
- B01D39/16—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres
- B01D39/1607—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres the material being fibrous
- B01D39/1623—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres the material being fibrous of synthetic origin
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
- B01D2239/04—Additives and treatments of the filtering material
- B01D2239/0435—Electret
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
- B01D2239/06—Filter cloth, e.g. knitted, woven non-woven; self-supported material
- B01D2239/065—More than one layer present in the filtering material
- B01D2239/0659—The layers being joined by needling
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
- B01D2239/12—Special parameters characterising the filtering material
- B01D2239/1258—Permeability
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2275/00—Filter media structures for filters specially adapted for separating dispersed particles from gases or vapours
- B01D2275/10—Multiple layers
Definitions
- the present embodiments relate generally to filter media and methods for filtering gas streams, and specifically, to filter media having efficiency stability and/or good performance characteristics such as low resistance.
- Filter elements can be used to remove contamination in a variety of applications.
- Such elements can include a filter media which may be formed of a web of fibers.
- the fiber web provides a porous structure that permits gas (e.g., air) to flow through the media.
- Contaminant particles e.g., dust particles, soot particles
- the filter media may be designed to have different performance characteristics.
- filter media for filtering particulates from air
- improvements in the physical and/or performance characteristics of the filter media e.g., strength, air resistance, efficiency, and high dust holding capacity
- Filter media are generally provided.
- the subject matter of this application involves, in some cases, interrelated products, alternative solutions to a particular problem, and/or a plurality of different uses of structures and compositions.
- a series of filter media comprises a first layer comprising a plurality of fibers, wherein the first layer comprises a fluorinated species, and a second layer adjacent the first layer.
- the first layer has a first value of a thickness over instantaneous resistance of the first layer
- the second layer has a second value of a thickness over instantaneous resistance of the second layer
- the ratio of the second value to the first value is less than or equal to 20.
- the filter media has an initial efficiency of greater than or equal to 95%.
- a filter media comprises a first layer comprising a plurality of fibers, wherein the first layer comprises a fluorinated species, and a second layer adjacent the first layer.
- the first layer has a value of thickness over instantaneous resistance of the first layer of greater than or equal to 2 mils/mmH 2 O and less than or equal to 50 mils/mm H 2 O.
- the second layer has a value of thickness over instantaneous resistance of the second layer of greater than or equal to 20 mils/mmH 2 O and less than or equal to 150 mils/mm H 2 O.
- a filter media comprises a first layer comprising a plurality of fibers and a second layer adjacent the first layer.
- the first layer has a first value of a thickness over instantaneous resistance of the first layer
- the second layer has a second value of a thickness over instantaneous resistance of the second layer
- the ratio of the second value to the first value is less than or equal to 20.
- the filter media has an initial efficiency of greater than or equal to 95%.
- a filter media comprises a first layer comprising a plurality of fibers and a second layer.
- the first layer has a first value of a basis weight over air permeability of the first layer
- the second layer has a second value of a basis weight over air permeability of the second layer
- the ratio of the first value to the second value is greater than or equal to 0.01 and less than or equal to 5 (e.g., greater than or equal to 0.01 and less than or equal to 4).
- the first layer has a basis weight of less than or equal to 20 g/m 2 and the plurality of fibers of the first layer have an average fiber diameter of greater than or equal to 1 micron and less than or equal to 8 microns.
- the second layer is charged and the second layer has a basis weight of greater than or equal to 30 g/m 2 and less than or equal to 85 g/m 2 .
- FIG. 1 is a schematic diagram showing a cross-section of a filter media according to one set of embodiments
- FIG. 2 is a schematic diagram showing a cross-section of a filter media according to one set of embodiments
- FIG. 3 is a schematic diagram showing a cross-section of a filter media according to one set of embodiments
- FIG. 4 is a schematic diagram showing a cross-section of a filter media according to one set of embodiments
- FIG. 5 is a schematic diagram showing a cross-section of a filter media according to one set of embodiments
- FIG. 6 is a plot of thickness over instantaneous resistance ratio of two layers of a filter media, according to one set of embodiments.
- FIG. 7 is a plot of air permeability versus basis weight over air permeability ratio of a filter media, according to one set of embodiments.
- Filter media such as multi-layered electret-containing filtration media for filtering gas streams (e.g., air) are described herein.
- the filter media may be designed to have desirable properties such as stable filtration efficiency, high oil repellency, low resistance, and/or stable service life.
- the filter media may be a composite of two or more types of fiber layers where each layer may be optimized to enhance its function without substantially negatively impacting the performance of another layer of the media. For example, one layer of the media may be designed to have a relatively high oil repellency, and another layer of the media may be designed to have stable filtration efficiency throughout the filter's lifetime.
- One or more layers of the media may have a certain value of thickness over instantaneous resistance (and/or a ratio of thickness over instantaneous resistance between two layers), as described in more detail below.
- the filter media described herein may be particularly well-suited for applications that involve filtering gas streams (e.g., face masks, cabin air filtration, vacuum filtration, room filtration, respirator equipment, as well as residential heating ventilation and air conditioning (HVAC) and industrial HVAC systems), though the media may also be used in other applications.
- filtering gas streams e.g., face masks, cabin air filtration, vacuum filtration, room filtration, respirator equipment, as well as residential heating ventilation and air conditioning (HVAC) and industrial HVAC systems
- one or more layers of the media may have a certain value of basis weight over air permeability (and/or a ratio of a value of basis weight over air permeability between two layers), as described in more detail below.
- the filter media may optionally comprise a support layer with a relatively high air permeability (e.g., greater than or equal to 1100 CFM).
- the filter may have a relatively low initial resistance and/or may have a particular final E1 efficiency according to the ASHRAE 52.2 standard described herein.
- the filter media may be needled together and in such embodiments does not comprise an adhesive or an adhesive layer, or is substantially free of adhesive.
- the filter media described herein may include a first layer, optionally including a fluorinated species, and a second layer that is charged.
- the first layer may be positioned upstream of the second layer (e.g., in a filter element) with respect to the direction of gas/fluid flow.
- the first layer may remove at least a portion of an oil present in a gas stream being filtered such that reduced amounts of the oil penetrates into the second layer, thereby minimizing discharge of the second layer. Since the presence of charges in the second layer can improve the efficiency (e.g., initial efficiency) of the media, this configuration of layers can stabilize the filtration efficiency of the filter media throughout its lifetime.
- the filter media described herein may advantageously have lower resistance leading to, for example, more breathability (e.g., for face mask applications) compared to certain existing filter media.
- the second layer may be positioned upstream of the first layer (e.g., in a filter element) with respect to the direction of gas/fluid flow.
- a filter media 100 may include a first layer 110 and a second layer 120 adjacent first layer 110 .
- first layer 110 may be directly adjacent (i.e., in direct contact with at least a portion of) second layer 120 .
- second layer 120 may be positioned upstream or downstream of, but not in contact with, first layer 110 .
- the first layer is a non-wet laid layer imparting, for example, good oleophobic properties (e.g., high oil repellency) to the filter media and the second layer may be a charged layer having, for example, high efficiency (e.g., initial efficiency) with a relatively open fibrous structure.
- good oleophobic properties e.g., high oil repellency
- the second layer may be a charged layer having, for example, high efficiency (e.g., initial efficiency) with a relatively open fibrous structure.
- the filter media includes one or more support layers (e.g., spunbond layers), as described in more detail below.
- first layer and second layer generally refer to different layers of a filter media and do not necessarily denote a particular order of the layers (e.g., within a filter element).
- a first layer may be positioned upstream of the second layer with respect to the direction of fluid flow, in other embodiments the first layer may be positioned downstream of the second layer with respect to the direction of fluid flow.
- first layer when a layer is referred to as being “adjacent” another layer, it can be directly adjacent to the layer, or one or more intervening layers also may be present.
- a layer that is “directly adjacent” another layer means that no intervening layer is present.
- each of the first layer and/or the second layer may include a single layer. In other embodiments, however, the first layer and/or the second layer may include more than one layer (i.e., sublayers) to form a multi-layered structure. Each sublayer within a layer may be formed by the same process as the other sublayers within the layer.
- a first layer includes more than one sublayers formed by a non-wet laid process such as a meltblown process, a meltspun, a melt electrospinning, a solvent electrospinning, a centrifugal spinning process, or a spunbond process.
- the plurality of sublayers may be the same or may differ based on certain features such as basis weight, efficiency (e.g., initial efficiency), and/or thickness. Generally, however, each sublayer within a given layer comprises the same type of fibers as the other sublayer(s) within the given layer.
- a first layer may include multiple sublayers, each sublayer including fibers formed by the same process (e.g., by a meltblown process).
- the plurality of sublayers may be discrete and combined by any suitable method, such as lamination, point bonding, or collating. In some embodiments, the sublayers are substantially joined to one another (e.g., by lamination, point bonding.
- thermo-dot bonding ultrasonic bonding, calendering, use of adhesives (e.g., glue-web), and/or co-pleating).
- adhesives e.g., glue-web
- sublayers may be formed as a composite layer (e.g., by a non-wet laid process).
- Each of the sublayers of the first layer and/or second layer may have any suitable basis weight and/or thickness, such as those basis weights and thicknesses described herein for the overall layer (e.g., the first layer, the second layer). Additionally, each of the sublayers of the first layer and/or second layer may have performance characteristics (e.g., resistance, efficiency) of those described herein for the overall layer.
- a layer of the filter media may comprise two or more sublayers.
- the first layer e.g., a non-wet laid layer
- the first layer may comprise two or more non-wet laid sublayers.
- filter media 102 shown in cross section, comprises a first layer 110 having a first non-wet laid sublayer 110 a and a second non-wet laid sublayer 110 b .
- the filter media also includes a second layer 120 adjacent first layer 110 .
- the second layer e.g., an efficiency layer and/or a charged layer
- filter media 104 comprises first layer 110 and second layer 120 adjacent first layer 110 , and having a first sublayer 120 a and a second sublayer 120 b . While two sublayers in each layer are shown, those skilled in the would understand that more than two sublayers (e.g., three sublayers, four sublayers, five sublayers) are also possible.
- a filter media 106 comprises first layer 110 having three non-wet laid sublayers 110 a , 110 b , and 110 c , and second layer 120 adjacent first layer 110 having three charged sublayers 120 a , 120 b , and 120 c . Other configurations are also possible.
- the first layer comprises greater than or equal to 1, greater than or equal to 2, greater than or equal to 3, greater than or equal to 5, greater than or equal to 7, greater than or equal to 10, or greater than or equal to 12 sublayers (e.g., non-wet laid sublayers). In certain embodiments, the first layer comprises less than or equal to 15, less than or equal to 12, less than or equal to 10, less than or equal to 7, less than or equal to 5, less than or equal to 3, or less than or equal to 2 sublayers.
- the second layer comprises greater than or equal to 1, greater than or equal to 2, greater than or equal to 3, greater than or equal to 5, greater than or equal to 7, greater than or equal to 10, or greater than or equal to 12 sublayers (e.g., charged sublayers). In certain embodiments, the second layer comprises less than or equal to 15, less than or equal to 12, less than or equal to 10, less than or equal to 7, less than or equal to 5, less than or equal to 3, or less than or equal to 2 sublayers.
- the first layer is designed to have a particular value of basis weight over air permeability of the first layer.
- the first layer may have a value of basis weight over air permeability of less than or equal to 0.2 g/m 2 /CFM and greater than or equal to 0.000125 g/m 2 /CFM or another suitable range described herein.
- a value of basis weight over air permeability for a particular layer, as used herein, is the ratio of the basis weight of the layer (including all sublayers of the layer) to the air permeability of the layer (including all sublayers of the layer). Measurements of basis weight and air permeability are described in more detail below.
- the first layer has a value of basis weight over air permeability of the first layer of less than or equal to 0.2 g/m 2 /CFM, less than or equal to 0.1 g/m 2 /CFM, less than or equal to 0.05 g/m 2 /CFM, less than or equal to 0.01 g/m 2 /CFM, less than or equal to 0.005 g/m 2 /CFM, less than or equal to 0.001 g/m 2 /CFM, less than or equal to 0.0005 g/m 2 /CFM, or less than or equal to 0.00025 g/m 2 /CFM.
- the first layer has a value of basis weight over air permeability of the first layer of greater than or equal to 0.000125 g/m 2 /CFM, greater than or equal to 0.00025 g/m 2 /CFM, greater than or equal to 0.0005 g/m 2 /CFM, greater than or equal to 0.001 g/m 2 /CFM, greater than or equal to 0.005 g/m 2 /CFM, greater than or equal to 0.01 g/m 2 /CFM, greater than or equal to 0.05 g/m 2 /CFM, or greater than or equal to 0.1 g/m 2 /CFM. Combinations of the above-referenced ranges are also possible (e.g., less than or equal to 0.2 g/m 2 /CFM and greater than or equal to 0.000125 g/m 2 /CFM). Other ranges are also possible.
- the first layer (including one or more sublayers of the first layer) may be designed to have a particular air permeability (e.g., such that the value of basis weight over air permeability of the first layer is greater than or equal to 0.000125 g/m 2 /CFM and less than or equal to 0.2 g/m 2 /CFM).
- a particular air permeability e.g., such that the value of basis weight over air permeability of the first layer is greater than or equal to 0.000125 g/m 2 /CFM and less than or equal to 0.2 g/m 2 /CFM).
- the air permeability of the first layer is greater than or equal to 100 CFM, greater than or equal to 200 CFM, greater than or equal to 250 CFM, greater than or equal to 300 CFM, greater than or equal to 350 CFM, greater than or equal to 400 CFM, greater than or equal to 450 CFM, greater than or equal to 500 CFM, greater than or equal to 550 CFM, greater than or equal to 600 CFM, greater than or equal to 650 CFM, greater than or equal to 700 CFM, or greater than or equal to 750 CFM.
- the air permeability of the first layer is less than or equal to 800 CFM, less than or equal to 750 CFM, less than or equal to 700 CFM, less than or equal to 650 CFM, less than or equal to 600 CFM, less than or equal to 550 CFM, less than or equal to 500 CFM, less than or equal to 450 CFM, less than or equal to 400 CFM, less than or equal to 350 CFM, less than or equal to 300 CFM, less than or equal to 250 CFM, or less than or equal to 200 CFM. Combinations of the above referenced ranges are also possible (e.g., greater than or equal to 100 CFM and less than or equal to 800 CFM, greater than or equal to 200 CFM and less than or equal to 650 CFM). Other ranges are also possible. Air permeability, as used herein, is measured according to the test standard ASTM D737 over 38 cm 2 surface area of the media and using a pressure of 125 Pa.
- the first layer is designed to have a particular value of thickness over instantaneous resistance of the layer (i.e., a thickness over instantaneous resistance factor).
- filter media comprising a first layer have a particular value of thickness over instantaneous resistance of the first layer (e.g., greater than or equal to 2 mils/mm H 2 O and less than or equal to 50 mils/mm H 2 O, or another suitable range described herein) which can increase the performance of filter media (e.g., lower resistance) as compared to certain existing filter media that do not have this feature.
- a value of thickness over instantaneous resistance is the ratio of the uncompressed thickness of a layer (including all sublayers of the layer) to the instantaneous resistance of the layer (including all sublayers of the layer). Measurements of uncompressed thickness and instantaneous resistance are described in more detail below.
- the first layer has a value of thickness over instantaneous resistance of the first layer of greater than or equal to 2 mils/mm H 2 O, greater than or equal to 3 mils/mm H 2 O, greater than or equal to 5 mils/mm H 2 O, greater than or equal to 10 mils/mm H 2 O, greater than or equal to 15 mils/mm H 2 O, greater than or equal to 20 mils/mm H 2 O, greater than or equal to 25 mils/mm H 2 O, greater than or equal to 30 mils/mm H 2 O, greater than or equal to 35 mils/mm H 2 O, greater than or equal to 40 mils/mm H 2 O, or greater than or equal to 45 mils/mm H 2 O.
- the first layer has a value of thickness over instantaneous resistance of the first layer of less than or equal to 50 mils/mm H 2 O, less than or equal to 45 mils/mm H 2 O, less than or equal to 40 mils/mm H 2 O, less than or equal to 35 mils/mm H 2 O, less than or equal to 30 mils/mm H 2 O, less than or equal to 25 mils/mm H 2 O, less than or equal to 20 mils/mm H 2 O, less than or equal to 15 mils/mm H 2 O, less than or equal to 10 mils/mm H 2 O, less than or equal to 5 mils/mm H 2 O, or less than or equal to 3 mils/mm H 2 O.
- the first layer (including one or more sublayers of the first layer) may be designed to have a particular uncompressed thickness (e.g., such that the thickness over instantaneous resistance factor of the first layer is greater than or equal to 2 mils/mm H 2 O and less than or equal to 50 mils/mm H 2 O).
- the uncompressed thickness of the first layer may be greater than or equal to 1 mil, greater than or equal to 2 mils, greater than or equal to 5 mils, greater than or equal to 10 mils, greater than or equal to 25 mils, greater than or equal to 50 mils, greater than or equal to 100 mils, greater than or equal to 200 mils, greater than or equal to 250 mils, greater than or equal to 300 mils, or greater than or equal to 400 mils.
- the uncompressed thickness of the first layer may be less than or equal to 500 mils, less than or equal to 400 mils, less than or equal to 300 mils, less than or equal to 250 mils, less than or equal to 200 mils, less than or equal to 100 mils, less than or equal to 50 mils, less than or equal to 25 mils, less than or equal to 10 mils, less than or equal to 5 mils, or less than or equal to 2 mils. Combinations of the above referenced ranges are also possible (e.g., greater than or equal to 1 mil and less than or equal to 500 mils, greater than or equal to 10 mils and less than or equal to 250 mils). Other ranges are also possible.
- Uncompressed thickness is determined using a Mitutoya uncompressed thickness measurement. Briefly, the fiber layer is compressed using a circular probe having a diameter of 1 mm under at least three different weights (e.g., 10 grams, 5 grams, 2 grams). The ordinary least squares linear regression is determined for each weight and corresponding thickness, and is used to calculated the thickness of the fiber layer corresponding to 0 grams of applied weight to determine the uncompressed thickness for that layer.
- weights e.g. 10 grams, 5 grams, 2 grams.
- the first layer may be designed to have a particular instantaneous resistance.
- the first layer may have an instantaneous resistance of less than or equal to 40 mm H 2 O, less than or equal to 35 mm H 2 O, less than or equal to 30 mm H 2 O, less than or equal to 25 mm H 2 O, less than or equal to 20 mm H 2 O, less than or equal to 15 mm H 2 O, less than or equal to 10 mm H 2 O, less than or equal to 5 mm H 2 O, or less than or equal to 2 mm H 2 O.
- the first layer may have an instantaneous resistance of greater than or equal to 0.1 mm H 2 O, greater than or equal to 0.2 mm H 2 O, greater than or equal to 0.5 mm H 2 O, greater than or equal to 1 mm H 2 O, greater than or equal to 2 mm H 2 O, greater than or equal to 5 mm H 2 O, greater than or equal to 10 mm H 2 O, greater than or equal to 15 mm H 2 O, greater than or equal to 20 mm H 2 O, greater than or equal to 25 mm H 2 O, greater than or equal to 30 mm H 2 O, or greater than or equal to 35 mm H 2 O.
- the first layer (or each sublayer of the first layer) has a particular instantaneous penetration.
- the instantaneous penetration of the first layer is less than or equal to 15%, less than or equal to 10%, less than or equal to 5%, less than or equal to 3%, less than or equal to 2%, less than or equal to 1%, or less than or equal to 0.5%.
- the instantaneous penetration of the first layer is greater than or equal to 0.01%, greater than or equal to 0.1%, greater than or equal to 0.5%, greater than or equal to 1%, greater than or equal to 2%, greater than or equal to 3%, greater than or equal to 5%, or greater than or equal to 10%. Combinations of the above-referenced ranges are also possible (e.g., less than or equal to 15% and greater than or equal to 0.01%). Other ranges are also possible. Measurements of instantaneous penetration are described below.
- the first layer (or each sublayer of the first layer) comprises a plurality of fibers.
- the fibers of the first layer (or each sublayer of the first layer) may be continuous or non-continuous.
- Continuous fibers and are made by a “continuous” fiber-forming process, such as a meltblown process, a meltspun, a melt electrospinning, a solvent electrospinning, a centrifugal spinning process, or a spunbond process, and typically have longer lengths than non-continuous fibers as described in more detail below.
- Non-continuous fibers are staple fibers that are generally cut (e.g., from a filament) or formed as non-continuous discrete fibers to have a particular length or a range of lengths as described in more detail below.
- the plurality of fibers of the first layer include synthetic fibers (synthetic polymer fibers).
- the synthetic fibers of the first layer may be continuous fibers or staple fibers.
- suitable synthetic fibers include polyester, polyaramid, polyimide, polyolefin (e.g., polyethylene), polypropylene, Kevlar, Nomex, halogenated polymers (e.g., polyethylene terephthalate), acrylics, polyphenylene oxide, polyphenylene sulfide, and combinations thereof.
- Synthetic fibers may also include multi-component fibers (i.e., fibers having multiple compositions such as bicomponent fibers).
- the synthetic fibers of the first layer are meltblown fibers, meltspun fibers, melt electrospun fibers, solvent electrospun fibers, centrifugal spun fibers, spunbond fibers, and/or combinations thereof, which may be formed of polymers described herein (e.g., polyester, polypropylene).
- Synthetic fibers of the first layer may also include staple fibers.
- the staple fibers may be multi-component fibers (i.e., fibers having multiple compositions such as bicomponent fibers).
- the layer may also include a binder (e.g., binder resin).
- a binder e.g., binder resin
- the plurality of fibers (e.g., synthetic fibers, continuous fibers, staple fibers) in the first layer (or in each sublayer of the first layer) may have an average diameter of greater than or equal to 0.2 microns, greater than or equal to 0.5 microns, greater than or equal to 1 micron, greater than or equal to 2 microns, greater than or equal to 3 microns, greater than or equal to 4 microns, greater than or equal to 5 microns, greater than or equal to 6 microns, greater than or equal to 8 microns, greater than or equal to 10 microns, greater than or equal to 15 microns, or greater than or equal to 20 microns.
- the plurality of fibers in the first layer may have an average diameter of less than or equal to 20 microns, less than or equal to 15 microns, less than or equal to 10 microns, less than or equal to 8 microns, less than or equal to 7 microns, less than or equal to 6 microns, less than or equal to 5 microns, less than or equal to 4 microns, less than or equal to 3 microns, less than or equal to 2 microns, less than or equal to 1 micron, or less than or equal to 0.5 microns.
- Combinations of the above-referenced ranges are also possible (e.g., greater than or equal to 0.2 micron and less than or equal to 20 microns, greater than or equal to 1 micron and less than or equal to about 10 microns, greater than or equal to 1 micron and less than or equal to 8 microns).
- Other values of average fiber diameter for the first layer (or each sublayer of the first layer) are also possible.
- the first layer comprises a plurality of fibers (e.g., synthetic fibers, continuous fibers) having a continuous length.
- the plurality of fibers in the first layer may have an average length of greater than about 5 inches, greater than or equal to about 10 inches, greater than or equal to about 25 inches, greater than or equal to about 50 inches, greater than or equal to about 100 inches, greater than or equal to about 300 inches, greater than or equal to about 500 inches, greater than or equal to about 700 inches, or greater than or equal to about 900 inches.
- the fibers may have an average length of less than or equal to about 1000 inches, less than or equal to about 800 inches, less than or equal to about 600 inches, less than or equal to about 400 inches, or less than or equal to about 100 inches. Combinations of the above-referenced ranges are also possible (e.g., greater than or equal to about 50 inches and less than or equal to about 1000 inches). Other ranges are also possible.
- the first layer comprises a plurality of fibers (e.g., synthetic fibers, staple fibers) having an average length of less than about 5 inches (127 mm).
- the plurality of fibers in the first layer may have an average length of, for example, less than or equal to about 100 mm, less than or equal to about 80 mm, less than or equal to about 60 mm, less than or equal to about 40 mm, less than or equal to about 20 mm, less than or equal to about 10 mm, less than or equal to about 5 mm, less than or equal to about 1 mm, less than or equal to about 0.5 mm, or less than or equal to about 0.1 mm.
- plurality of fibers in the first layer may have an average length of greater than or equal to about 0.02 mm, greater than or equal to about 0.1 mm, greater than or equal to about 0.5 mm, greater than or equal to about 1 mm, greater than or equal to about 5 mm, greater than or equal to about 10 mm, greater than or equal to about 20 mm, greater than or equal to about 40 mm, greater than or equal to about 60 mm. Combinations of the above-referenced ranges are possible (e.g., greater than or equal to about 0.02 mm and less than or equal to about 80 mm, greater than or equal to about 0.03 mm and less than or equal to about 40 mm). Other ranges are also possible.
- the first layer may have certain structural characteristics, such as basis weight and/or solidity.
- the first layer (or each of the sub-layers of the first layer) may have a basis weight of greater than or equal to 0.1 g/m 2 , greater than or equal to 0.5 g/m 2 , greater than or equal to 1 g/m 2 , greater than or equal to 3 g/m 2 , greater than or equal to 10 g/m 2 , greater than or equal to 25 g/m 2 , greater than or equal to 30 g/m 2 , greater than or equal to 40 g/m 2 , greater than or equal to 50 g/m 2 , greater than or equal to 60 g/m 2 , greater than or equal to 70 g/m 2 , greater than or equal to 80 g/m 2 , greater than 85 g/m 2 , greater than or equal to 90 g/m 2 , greater than or equal to 100 g/m 2 , greater than or equal
- the first layer (or each of the sub-layers of the first layer) may have a basis weight of less than or equal to 500 g/m 2 , less than or equal to 400 g/m 2 , less than or equal to 300 g/m 2 , less than or equal to 200 g/m 2 , less than or equal to 100 g/m 2 , less than or equal to 90 g/m 2 , less than or equal to 85 g/m 2 , less than or equal to 80 g/m 2 , less than or equal to 70 g/m 2 , less than or equal to 60 g/m 2 , less than or equal to 50 g/m 2 , less than or equal to 40 g/m 2 , less than or equal to 30 g/m 2 , less than or equal to 25 g/m 2 , less than or equal to 10 g/m 2 , less than or equal to 3 g/m 2 , less than or equal to 1 g/m 2 , or less than or equal to
- a basis weight of greater than or equal to 0.1 g/m 2 and less than or equal to 500 g/m 2 e.g., a basis weight of greater than or equal to 10 g/m 2 and less than or equal to 250 g/m 2 , a basis weight of greater than or equal to 6 g/m 2 and less than or equal to 80 g/m 2 , a basis weight of greater than or equal to 0.1 g/m 2 and less than or equal to 20 g/m 2 ).
- the basis weight may be determined according to the standard ISO 536.
- the first layer has a basis weight of less than or equal to 20 g/m 2 .
- the first layer (or each of the sub-layers of the first layer) may have a solidity of greater than or equal to 0.1%, greater than or equal to 0.5%, greater than or equal to 1%, greater than or equal to 5%, greater than or equal to 10%, greater than or equal to 20%, or greater than or equal to 40%. In certain embodiments, the first layer (or each of the sub-layers of the first layer) may have a solidity of less than or equal to 50%, less than or equal to 40%, less than or equal to 30%, less than or equal to 20%, less than or equal to 10%, less than or equal to 5%, less than or equal to 1%, or less than or equal to 0.5%.
- Solidity generally refers to the percentage of volume of solids with respect to the total volume of the layer.
- the first layer (or one or more sublayers of the first layer) comprises a fluorinated species.
- each sublayer of the first layer comprises a fluorinated species.
- the fluorinated species may impart a certain level of oil repellency to the media.
- Non-limiting examples of fluorinated species include fluorocarbons such as those having the formula —C n F 2n+1 or —C n F m , where n is an integer greater than 1, and m is an integer greater than 1. In some embodiments, n is less than or equal to 8, less than or equal 6, less than or equal 5, or less than or equal to 4.
- m is less than or equal to 14, less than or equal to 13, less than or equal to 12, less than or equal to 8, less than or equal 6, less than or equal 5, or less than or equal to 4.
- fluorocarbons include CF 4 , C 2 F 4 , C 3 F 6 , C 3 F 8 , C 4 F 8 , C 5 F 12 , C 6 F 6 , C 6 F 12 , and C 6 F 13 .
- fluorinated species include fluorocarbons such as those having the formula C n F m —(C x H y )—Z, where n is an integer equal or greater than 1, m is an integer equal or greater than 1, x is an integer greater than 0, y is an integer greater than 0, and Z is an end functional group that can be selected from the group consisting of acrylate, methacrylate, alcohol, aldehyde, carboxylic acid, olefins, silane, bromide, iodide, thiol, amine, phenol, isocyanate, sulfonate, epoxide, and ether.
- fluorocarbons such as those having the formula C n F m —(C x H y )—Z, where n is an integer equal or greater than 1, m is an integer equal or greater than 1, x is an integer greater than 0, y is an integer greater than 0, and Z is an end functional group that can be selected from the group consisting of
- n is less than or equal to 11, less than or equal to 8, less than or equal 6, less than or equal 5, or less than or equal to 4.
- m is less than or equal to 14, less than or equal to 13, less than or equal to 12, less than or equal to 8, less than or equal 6, less than or equal 5, or less than or equal to 4.
- x is less than or equal to 12, less than or equal to 8, less than or equal 6, less than or equal 5, or less than or equal to 4.
- y is less than or equal to 25, less than or equal to 20, less than or equal to 15, less than or equal to 10, less than or equal to 8, less than or equal 6, less than or equal 5, or less than or equal to 4.
- the value of m may vary depending on the value of n, and the value of y may depend on the value of x.
- —(C x H y )— is a linear alkane or a branched alkane.
- one or more fluorinated species are present in the first layer (e.g., as a coating) in an amount of greater than or equal to 0.01%, greater than or equal to 0.05%, greater than or equal to 0.1%, greater than or equal to 0.5%, greater than or equal to 0.75%, greater than or equal to 1%, greater than or equal to 2%, greater than or equal to 3%, or greater than or equal to 5% by weight of the total dry weight of the first layer.
- one or more fluorinated species are present in the first layer (e.g., as a coating) in an amount of less than or equal to 10%, less than or equal to 5%, less than or equal to 3%, less than or equal to 2%, less than or equal to 1%, less than or equal to 0.75%, less than or equal to 0.5%, less than or equal to 0.1%, or less than or equal to 0.05% by weight of the total dry weight of the first layer.
- Combinations of the above referenced ranges are also possible (e.g., greater than or equal to 0.01% and less than or equal to 10%, greater than or equal to 0.01% and less than or equal to 5%, greater than or equal to 0.05% and less than or equal to 3%, greater than or equal to 0.1% and less than or equal to 2%, greater than or equal to 0.2% and less than or equal to 0.75%).
- Other ranges are also possible.
- the first layer, or one or more sublayers of the first layer may be modified to comprise a fluorinated species using any suitable method.
- the entire layer may be modified (e.g., through its thickness).
- the interior and the surfaces of the layer (or one or more sublayers of the layer) may be modified with a fluorinated species.
- the interior of the layer (or one or more sublayers of the layer) may be modified without one or more outer surfaces of the layer (or one or more sublayers of the layer) being modified.
- any suitable method for modifying the surface and/or the interior of a layer (or one or more sublayers of the layer) may be used.
- a coating method is used to coat a layer with a fluorinated species.
- filter media may undergo a coating process (e.g., chemical vapor deposition), such that one or more outer surfaces of an interior layer and/or bottom layer is not coated, while the porous interior of the layer is coated.
- the surface and/or interior of a layer (or one or more sublayers of the layer) may be modified by coating at least a portion of the surface and/or interior.
- a coating process involves introducing resin or a material (e.g., a fluorinated species) dispersed in a solvent or solvent mixture into a pre-formed fiber layer (e.g., a pre-formed fiber layer formed by a meltblown process, etc.).
- a material e.g., a fluorinated species
- a pre-formed fiber layer e.g., a pre-formed fiber layer formed by a meltblown process, etc.
- Non-limiting examples of coating methods include the use of vapor deposition (e.g., chemical vapor, physical vapor deposition), layer-by-layer deposition, wax-solidification, self-assembly, sol-gel processing, a slot die coater, gravure coating, screen coating, size press coating (e.g., a two roll-type or a metering blade type size press coater), film press coating, blade coating, roll-blade coating, air knife coating, roll coating, foam application, reverse roll coating, bar coating, curtain coating, champlex coating, brush coating, Bill-blade coating, short dwell-blade coating, lip coating, gate roll coating, gate roll size press coating, laboratory size press coating, melt coating, dip coating, knife roll coating, spin coating, spray coating (e.g., electrospraying), gapped roll coating, roll transfer coating, padding saturant coating, and saturation impregnation.
- vapor deposition e.g., chemical vapor, physical vapor deposition
- layer-by-layer deposition e.
- the first layer described herein may be modified using chemical vapor deposition (e.g., chemical vapor deposition of a fluorinated species).
- chemical vapor deposition the fiber layer is exposed to gaseous reactants from gas or liquid vapor that are deposited onto the fiber layer under high energy level excitation such as thermal, microwave, UV, electron beam or plasma.
- a carrier gas such as oxygen, helium, argon and/or nitrogen may be used.
- vapor deposition methods include atmospheric pressure chemical vapor deposition (APCVD), low pressure chemical vapor deposition (LPCVD), metal-organic chemical vapor deposition (MOCVD), plasma assisted chemical vapor deposition (PACVD) or plasma enhanced chemical vapor deposition (PECVD), laser chemical vapor deposition (LCVD), photochemical vapor deposition (PCVD), chemical vapor infiltration (CVI) and chemical beam epitaxy (CBE).
- APCVD atmospheric pressure chemical vapor deposition
- LPCVD low pressure chemical vapor deposition
- MOCVD metal-organic chemical vapor deposition
- PCVD plasma assisted chemical vapor deposition
- PECVD plasma enhanced chemical vapor deposition
- LCVD laser chemical vapor deposition
- PCVD photochemical vapor deposition
- CVI chemical vapor infiltration
- CBE chemical beam epitaxy
- PVD physical vapor deposition
- the coating may be dried or cured by any suitable method.
- drying or curing methods include the use of a photo dryer, infrared dryer, ultraviolet source, electron beam, hot air oven steam-heated cylinder, or any suitable type of dryer familiar to those of ordinary skill in the art.
- the first layer (and any sublayers), the second layer, and/or the entire media does not include a fluorinated species (e.g., does not comprise a coating such as a chemical vapor deposition coating comprising a fluorinated species).
- the first layer, or one or more sublayers of the first layer may be, in some cases, charged.
- the first layer comprises a plurality of charged fibers.
- the first layer (or one or more sublayers of the first layer) is/are not charged.
- a filter media may include a second layer with optional sublayers.
- the second layer is an efficiency layer (i.e., it increases the efficiency/initial efficiency of the overall media).
- the second layer is a charged layer (an electret layer).
- the second layer is designed to have a particular value of basis weight over air permeability of the second layer.
- filter media comprising a second layer have a particular value of basis weight over air permeability of the second layer (e.g., greater than or equal to 0.03 g/m 2 /CFM and less than or equal to 0.25 g/m 2 /CFM, or another suitable range described herein).
- a value of basis weight over air permeability is the ratio of the basis weight (including all sublayers of the layer) to the air permeability (including all sublayers of the layer). Measurements of basis weight and air permeability are described herein.
- the second layer has a value of basis weight over air permeability of the second layer of less than or equal to 0.25 g/m 2 /CFM, less than or equal to 0.2 g/m 2 /CFM, less than or equal to 0.175 g/m 2 /CFM, less than or equal to 0.15 g/m 2 /CFM, less than or equal to 0.125 g/m 2 /CFM, less than or equal to 0.1 g/m 2 /CFM, less than or equal to 0.09 g/m 2 /CFM, less than or equal to 0.07 g/m 2 /CFM, less than or equal to 0.05 g/m 2 /CFM, or less than or equal to 0.04 g/m 2 /CFM.
- the second layer has a value of basis weight over air permeability of the second layer of greater than or equal to 0.03 g/m 2 /CFM, greater than or equal to 0.04 g/m 2 /CFM, greater than or equal to 0.05 g/m 2 /CFM, greater than or equal to 0.07 g/m 2 /CFM, greater than or equal to 0.09 g/m 2 /CFM, greater than or equal to 0.1 g/m 2 /CFM, greater than or equal to 0.125 g/m 2 /CFM, greater than or equal to 0.15 g/m 2 /CFM, greater than or equal to 0.175 g/m 2 /CFM, or greater than or equal to 0.2 g/m 2 /CFM. Combinations of the above-referenced ranges are also possible (e.g., greater than or equal to 0.03 g/m 2 /CFM and less than or equal to 0.25 g/m 2 /CFM). Other ranges are also possible (e
- the second layer (including one or more sublayers of the second layer) may be designed to have a particular air permeability (e.g., such that the value of basis weight over air permeability of the second layer is greater than or equal to 0.03 g/m 2 /CFM and less than or equal to 0.25 g/m 2 /CFM).
- a particular air permeability e.g., such that the value of basis weight over air permeability of the second layer is greater than or equal to 0.03 g/m 2 /CFM and less than or equal to 0.25 g/m 2 /CFM).
- the air permeability of the second layer is greater than or equal to 200 CFM, greater than or equal to 250 CFM, greater than or equal to 300 CFM, greater than or equal to 330 CFM, greater than or equal to 350 CFM, greater than or equal to 400 CFM, greater than or equal to 500 CFM, greater than or equal to 600 CFM, greater than or equal to 650 CFM, greater than or equal to 700 CFM, greater than or equal to 800 CFM, or greater than or equal to 900 CFM.
- the air permeability of the second layer is less than or equal to 1000 CFM, less than or equal to 900 CFM, less than or equal to 800 CFM, less than or equal to 700 CFM, less than or equal to 600 CFM, less than or equal to 500 CFM, less than or equal to 400 CFM, less than or equal to 350 CFM, less than or equal to 330 CFM, less than or equal to 300 CFM, or less than or equal to 250 CFM. Combinations of the above referenced ranges are also possible (e.g., greater than or equal to 200 CFM and less than or equal to 1000 CFM, greater than or equal to 330 CFM and less than or equal to 1000 CFM). Other ranges are also possible.
- the second layer is designed to have a particular thickness over instantaneous resistance factor.
- filter media comprising a second layer have a particular value of thickness over instantaneous resistance of the second layer (e.g., greater than or equal to 20 mils/mm H 2 O and less than or equal to 150 mils/mm H 2 O, or another suitable range as described herein), which can increase the performance of filter media (e.g., lower resistance) as compared to certain existing filter media that do not have this feature.
- the second layer has a value of thickness over instantaneous resistance of the second layer (i.e., a thickness over instantaneous resistance factor) of greater than or equal to 20 mils/mm H 2 O, greater than or equal to 30 mils/mm H 2 O, greater than or equal to 40 mils/mm H 2 O, greater than or equal to 50 mils/mm H 2 O mils/mm H 2 O, greater than or equal to 75 mils/mm H 2 O, greater than or equal to 100 mils/mm H 2 O, or greater than or equal to 125 mils/mm H 2 O.
- a thickness over instantaneous resistance factor of greater than or equal to 20 mils/mm H 2 O, greater than or equal to 30 mils/mm H 2 O, greater than or equal to 40 mils/mm H 2 O, greater than or equal to 50 mils/mm H 2 O mils/mm H 2 O, greater than or equal to 75 mils/mm H 2 O, greater than or equal to 100 mils/mm H 2 O, or greater than or equal to
- the second layer has a thickness over instantaneous resistance factor of less than or equal to 150 mils/mm H 2 O, less than or equal to 125 mils/mm H 2 O, less than or equal to 100 mils/mm H 2 O, less than or equal to 75 mils/mm H 2 O, less than or equal to 50 mils/mm H 2 O, less than or equal to 40 mils/mm H 2 O, or less than or equal to 30 mils/mm H 2 O.
- the second layer may be designed to have a particular uncompressed thickness (e.g., such that the thickness over instantaneous resistance factor of the second layer is greater than or equal to 20 mils/mm H 2 O and less than or equal to 150 mils/mm H 2 O).
- the uncompressed thickness of the second layer may be greater than or equal to 5 mils, greater than or equal to 10 mils, greater than or equal to 25 mils, greater than or equal to 30 mils, greater than or equal to 50 mils, greater than or equal to 100 mils, greater than or equal to 200 mils, greater than or equal to 250 mils, greater than or equal to 300 mils, greater than or equal to 350 mils, greater than or equal to 400 mils, or greater than or equal to 500 mils.
- the uncompressed thickness of the second layer may be less than or equal to 600 mils, less than or equal to 500 mils, less than or equal to 400 mils, less than or equal to 350 mils, less than or equal to 300 mils, less than or equal to 250 mils, less than or equal to 200 mils, less than or equal to 100 mils, less than or equal to 50 mils, less than or equal to 30 mils, less than or equal to 25 mils, or less than or equal to 10 mils. Combinations of the above referenced ranges are also possible (e.g., greater than or equal to 5 mils and less than or equal to 600 mils, greater than or equal to 30 mils and less than or equal to 350 mils). Other ranges are also possible.
- the second layer may be designed to have a particular instantaneous resistance.
- the second layer may have an instantaneous resistance of greater than or equal to 0.1 mm H 2 O, greater than or equal to 0.2 mm H 2 O, greater than or equal to 0.5 mm H 2 O, greater than or equal to 1 mm H 2 O, greater than or equal to 2 mm H 2 O, or greater than or equal to 5 mm H 2 O.
- the second layer may have an instantaneous resistance of less than or equal to 10 mm H 2 O, less than or equal to 5 mm H 2 O, or less than or equal to 2 mm H 2 O.
- the second layer (or each sublayer of the second layer) as a particular instantaneous penetration.
- the instantaneous penetration of the second layer is less than or equal to 50%, less than or equal to 45%, less than or equal to 40%, less than or equal to 35%, less than or equal to 30%, less than or equal to 25%, less than or equal to 20%, less than or equal to 15%, less than or equal to 10%, less than or equal to 5%, less than or equal to 3%, less than or equal to 2%, less than or equal to 1%, or less than or equal to 0.5%.
- the instantaneous penetration of the second layer is greater than or equal to 0.01%, greater than or equal to 0.1%, greater than or equal to 0.5%, greater than or equal to 1%, greater than or equal to 2%, greater than or equal to 3%, greater than or equal to 5%, greater than or equal to 10%, greater than or equal to 20%, greater than or equal to 30%, or greater than or equal to 40%. Combinations of the above-referenced ranges are also possible (e.g., less than or equal to 15% and greater than or equal to 0.01%, less than or equal to 50% and greater than or equal to 0.01%). Other ranges are also possible. Measurements of instantaneous penetration are described below.
- the second layer (or each sublayer of the second layer) comprises a plurality of fibers.
- the fibers of the second layer (or each sublayer of the second layer) may be non-continuous (e.g., staple fibers) or continuous, and may be optionally charged. Accordingly, the second layer may be charged in some embodiments.
- the plurality of fibers of the second layer include synthetic fibers (synthetic polymer fibers).
- the synthetic fibers of the second layer may be staple fibers or continuous fibers.
- Non-limiting examples of suitable synthetic fibers include polypropylene, dry-spun acrylic (e.g., produced from a dry-spinning process), polyvinyl chloride, mod-acrylic, wet spun acrylic, polytetrafluoroethylene, polypropylene, polystyrene, polysulfone, polyethersulfone, polycarbonate, nylon (e.g., nylon 6/6), polyurethane, phenolic, polyvinylidene fluoride, polyester, polyaramid, polyimide, polyolefin (e.g., polyethylene), Kevlar, Nomex, halogenated polymers (e.g., polyethylene terephthalate), polyacrylics, polyphenylene oxide, polyphenylene sulfide, and combinations thereof.
- suitable synthetic fibers include polypropylene, dry-spun acrylic (e.g., produced from a dry-spinning process), polyvinyl chloride, mod-acrylic, wet spun acrylic, polyte
- the synthetic fibers are halogen-free such that significant dioxins are not detectable when incinerated.
- the fibers may be halogen-free acrylic fibers formed by dry spinning.
- the second layer and/or the entire filter media is halogen-free such that significant dioxins are not detectable when incinerated.
- the plurality of fibers in the second layer are staple fibers that are synthetic polymer fibers, and are carded.
- the fibers of the second layer may be charged.
- the plurality of fibers in the second layer include synthetic fibers (synthetic polymer fibers) formed by a continuous fiber-forming process such as a meltblown process, a meltspun, a melt electrospinning, a solvent electrospinning, a centrifugal spinning process, or a spunbond process.
- the synthetic fibers are meltblown fibers, meltspun fibers, melt electrospun fibers, solvent electrospun fibers, centrifugal spun fibers, spunbond fibers, and/or combinations thereof.
- Synthetic fibers may also include multi-component fibers (i.e., fibers having multiple compositions such as bicomponent fibers).
- synthetic fibers may include meltblown fibers, which may be formed of polymers described herein (e.g., polyester, polypropylene). Other processes and materials used to form the second layer are also possible. The fibers of the second layer may be charged.
- the second layer comprises a mixture of two or more polymeric fibers.
- the second layer may comprise at least a first plurality of fibers comprising a first polymer and a second plurality of fibers comprising a second polymer.
- the first polymer and the second polymer are selected such that the first polymer and the second polymer have different dielectric constants.
- the two polymers having different dielectric constants may facilitate charging of the layer (e.g., triboelectric charging).
- two polymers with different dielectric constants in the layer may come into frictional contact during manufacture of the layer such that one polymer will lose electrons and give them away to the other polymer and, as a result, the polymer losing electrons is net positively charged, the other polymer receiving electrons is net negatively charged.
- the charged layer may have one or more characteristics described in commonly-owned U.S. Pat. No. 6,623,548, entitled “Filter materials and methods for the production thereof”, issued Sep. 23, 2003, which is incorporated herein by reference in its entirety for all purposes.
- the second layer is an electrostatically charged layer formed by blending together polypropylene fibers with halogen free acrylic fibers, polypropylene with polyvinyl chloride (PVC) fibers, or a mixture of halogen free acrylic fibers and PVC fibers and, optionally, carding the blended fibers so as to form a non-woven fabric.
- PVC polyvinyl chloride
- the difference in dielectric constants between the first polymer and the second polymer may be selected to be greater than or equal to 0.8, greater than or equal to 1, greater than or equal to 1.2, greater than or equal to 1.5, greater than or equal to 2, greater than or equal to 3, greater than or equal to 5, or greater than or equal to 7.
- the difference in dielectric constants between the first polymer and the second polymer may be selected to be less than or equal to 8, less than or equal to 7, less than or equal to 5, less than or equal to 3, less than or equal to 2, less than or equal to 1.5, less than or equal to 1.2, or less than or equal to 1. Combinations of the above-referenced ranges are also possible (e.g., greater than or equal to 0.8 and less than or equal to 8, greater than or equal to 1.5 and less than or equal to 5). Other ranges are also possible.
- Table 1 shows dielectric constants for several exemplary polymers.
- the first polymer and the second polymer may be present in the second layer (or in each of the sublayers of the second layer) in any suitable amount.
- the first polymer is present in the second layer (or in each of the sublayers of the second layer) in an amount of greater than or equal to 25 wt %, greater than or equal to 30 wt %, greater than or equal to 35 wt %, greater than or equal to 40 wt %, greater than or equal to 50 wt %, greater than or equal to 60 wt %, greater than or equal to 65 wt %, or greater than or equal to 70 wt % with respect to the total amount of fibers in the layer and/or the total weight of the layer.
- the first polymer is present in the second layer in an amount of less than or equal to 75 wt %, less than or equal to 70 wt %, less than or equal to 65 wt %, less than or equal to 60 wt %, less than or equal to 50 wt %, less than or equal to 40 wt %, less than or equal to 35 wt %, or less than or equal to 30 wt % with respect to the total amount of fibers in the layer and/or the total weight of the layer. Combinations of the above referenced ranges are also possible (e.g., greater than or equal to 25 wt % and less than or equal to 75 wt %). Other ranges are also possible.
- the second polymer is present in the second layer (or in each of the sublayers of the second layer) in an amount of less than or equal to 75 wt %, less than or equal to 70 wt %, less than or equal to 65 wt %, less than or equal to 60 wt %, less than or equal to 50 wt %, less than or equal to 40 wt %, less than or equal to 35 wt %, or less than or equal to 30 wt % with respect to the total amount of fibers in the layer and/or the total weight of the layer.
- the second polymer is present in the second layer in an amount of greater than or equal to 25 wt %, greater than or equal to 30 wt %, greater than or equal to 35 wt %, greater than or equal to 40 wt %, greater than or equal to 50 wt %, greater than or equal to 60 wt %, greater than or equal to 65 wt %, or greater than or equal to 70 wt % with respect to the total amount of fibers in the layer and/or the total weight of the layer. Combinations of the above referenced ranges are also possible (e.g., greater than or equal to 25 wt % and less than or equal to 75 wt %). Other ranges are also possible.
- the second layer comprises the first polymer in an amount of greater than or equal to about 25 wt % and less than or equal to 75 wt % and the second polymer in an amount of less than or equal to 75 wt % and greater than or equal to about 25 wt % with respect to the total amount of fibers in the layer.
- the second layer may comprise the first polymer in an amount of greater than or equal to about 45 wt % and less than or equal to 55 wt %, and the second polymer in an amount of less than or equal to 55 wt % and greater than or equal to about 45 wt %, with respect to the total amount of fibers in the layer.
- the second layer comprises each of the first polymer and the second polymer in an amount of about 50 wt % with respect to the total amount of fibers in the layer.
- the second layer comprises a plurality of fibers (e.g., synthetic fibers, staple fibers) having an average length of less than about 5 inches (127 mm).
- the plurality of fibers in the second layer may have an average length of, for example, less than or equal to about 100 mm, less than or equal to about 80 mm, less than or equal to about 60 mm, less than or equal to about 40 mm, less than or equal to about 20 mm, less than or equal to about 10 mm, less than or equal to about 5 mm, less than or equal to about 1 mm, less than or equal to about 0.5 mm, or less than or equal to about 0.1 mm.
- plurality of fibers in the second layer may have an average length of greater than or equal to about 0.02 mm, greater than or equal to about 0.1 mm, greater than or equal to about 0.5 mm, greater than or equal to about 1 mm, greater than or equal to about 5 mm, greater than or equal to about 10 mm, greater than or equal to about 20 mm, greater than or equal to about 40 mm, greater than or equal to about 60 mm. Combinations of the above-referenced ranges are possible (e.g., greater than or equal to about 1 mm and less than or equal to about 80 mm, greater than or equal to about 1 mm and less than or equal to about 60 mm). Other ranges are also possible.
- the second layer comprises a plurality of fibers (e.g., synthetic fibers, continuous fibers) having a continuous length.
- the plurality of fibers in the second layer may have an average length of greater than about 5 inches, greater than or equal to about 10 inches, greater than or equal to about 25 inches, greater than or equal to about 50 inches, greater than or equal to about 100 inches, greater than or equal to about 300 inches, greater than or equal to about 500 inches, greater than or equal to about 700 inches, or greater than or equal to about 900 inches.
- the fibers may have an average length of less than or equal to about 1000 inches, less than or equal to about 800 inches, less than or equal to about 600 inches, less than or equal to about 400 inches, or less than or equal to about 100 inches. Combinations of the above-referenced ranges are also possible (e.g., greater than or equal to about 50 inches and less than or equal to about 1000 inches).
- the second layer may have certain structural characteristics, such as basis weight and/or solidity.
- the second layer (or each of the sub-layers of the second layer) may have a basis weight of greater than or equal to 20 g/m 2 , greater than or equal to 25 g/m 2 , greater than or equal to 30 g/m 2 , greater than or equal to 40 g/m 2 , greater than or equal to 50 g/m 2 , greater than or equal to 60 g/m 2 , greater than or equal to 70 g/m 2 , greater than or equal to 80 g/m 2 , greater than or equal to 85 g/m 2 , greater than or equal to 90 g/m 2 , greater than or equal to 100 g/m 2 , greater than or equal to 200 g/m 2 , greater than or equal to 300 g/m 2 , greater than or equal to 400 g/m 2 , or greater than or equal to 500 g/m 2 .
- the second layer (or each of the sub-layers of the second layer) may have a basis weight of less than or equal to 600 g/m 2 , less than or equal to 500 g/m 2 , less than or equal to 400 g/m 2 , less than or equal to 300 g/m 2 , less than or equal to 200 g/m 2 , less than or equal to 100 g/m 2 , less than or equal to 90 g/m 2 , less than or equal to 85 g/m 2 , less than or equal to 80 g/m 2 , less than or equal to 70 g/m 2 , less than or equal to 60 g/m 2 , less than or equal to 50 g/m 2 , less than or equal to 40 g/m 2 , or less than or equal to 30 g/m 2 .
- the basis weight may be determined as described above.
- the second layer has a basis weight of greater than or equal to 30 g/m 2 and less than or equal to 85 g/m 2 .
- the second layer (or each of the sub-layers of the second layer) may have a solidity of greater than or equal to 0.1%, greater than or equal to 0.5%, greater than or equal to 1.0%, greater than or equal to 5.0%, greater than or equal to 10%, greater than or equal to 20%, or greater than or equal to 40%. In certain embodiments, the second layer (or each of the sub-layers of the second layer) may have a solidity of less than or equal to 50%, less than or equal to 40%, less than or equal to 20%, less than or equal to 10%, less than or equal to 5%, less than or equal to 1%, or less than or equal to 0.5%. Combinations of the above-referenced ranges are also possible (e.g., a solidity of greater than or equal to 0.1% and less than or equal to 50%, greater than or equal to 1% and less than or equal to 20%). Other ranges are also possible.
- the filter media may be a multi-layered electret-containing media.
- a layer e.g., a second layer
- the net charge of the layer may be negative or positive.
- at least a surface of the second layer may comprise a negatively charged material and/or a positively charged material.
- the polymers in the second layer may be selected based on their dielectric constant and/or position on the triboelectric series, as described herein.
- the second layer is formed via a carding process (e.g., where the fibers are manipulated by rollers and extensions (e.g., hooks, needles)).
- the polymer fibers within the second layer with a significant difference in dielectric constant and/or that are relatively far apart on the triboelectric series may undergo contact electrification as a result of the carding process to produce a charged non-woven web.
- Charged non-woven webs may have enhanced performance properties, including an increased efficiency, compared to a similar non-woven web that is uncharged, all other factors being equal.
- a layer may be neutral (e.g., have no net charge).
- the filter media described herein may have a relatively low pressure drop (i.e., resistance) and/or a relatively long lifetime as compared to certain existing filter media.
- the filter media may have a decrease in resistance (e.g., initial resistance) when the media includes at least two layers, wherein the ratio of the value of thickness over instantaneous resistance of the second layer to the value of thickness over instantaneous resistance of the first layer (i.e., a TRF ratio) is less than or equal 20.
- the media passes a P95 filter media test as described in more detail below.
- the filter media described herein may have a relatively low pressure drop (i.e., resistance) as compared to certain existing filter media when the media includes at least two layers and the ratio of the value of basis weight over air permeability of the first layer to the value of the basis weight over air permeability of the second layer less than or equal to 5 (e.g., less than or equal to 4).
- the filter media may have a ratio of the value of basis weight over air permeability of the first layer to the value of basis weight over air permeability of the second layer (WOA ratio) of less than or equal to 5, less than or equal to 4, less than or equal to 3, less than or equal to 2, less than or equal to 1, less than or equal to 0.5, less than or equal to 0.25, less than or equal to 0.2, less than or equal to 0.1, less than or equal to 0.05, or less than or equal to 0.02.
- WOA ratio ratio of the value of basis weight over air permeability of the first layer to the value of basis weight over air permeability of the second layer
- the filter media may have a ratio of the value of basis weight over air permeability of the first layer to the value of basis weight over air permeability of the second layer of greater than or equal to 0.01, greater than or equal to 0.02, greater than or equal to 0.05, greater than or equal to 0.1, greater than or equal to 0.2, greater than or equal to 0.25, greater than or equal to 0.5, greater than or equal to 1, greater than or equal to 2, greater than or equal to 3, or greater than or equal to 4. Combinations of the above referenced ranges are also possible (e.g., greater than or equal to 0.01 and less than or equal to 5, greater than or equal to 0.02 and less than or equal to 3). Other ranges are also possible.
- the filter media may have a particular composite air permeability.
- Composite air permeability refers to the total air permeability of a filter media comprising at least a first layer and a second layer, and is measured according to the ASTM D737 test described herein.
- the composite air permeability of the filter media is greater than or equal to 200 CFM, greater than or equal to 250 CFM, greater than or equal to 300 CFM, greater than or equal to 350 CFM, greater than or equal to 400 CFM, greater than or equal to 450 CFM, greater than or equal to 500 CFM, or greater than or equal to 550 CFM.
- the composite air permeability of the filter media is less than or equal to 600 CFM, less than or equal to 550 CFM, less than or equal to 500 CFM, less than or equal to 450 CFM, less than or equal to 400 CFM, less than or equal to 350 CFM, less than or equal to 300 CFM, or less than or equal to 250 CFM. Combinations of the above referenced ranges are also possible (e.g., greater than or equal to 200 CFM and less than or equal to 600 CFM). Other ranges are also possible.
- a filter media described herein may have a particular final E1 efficiency (e.g., a final E1 efficiency of greater than or equal to 36%), according to the ASHRAE 52.2 standard.
- the final E1 efficiency of the filter media is greater than or equal to 36%, greater than or equal to 40%, greater than or equal to 50%, greater than or equal to 60%, greater than or equal to 70%, greater than or equal to 80%, greater than or equal to 90%, greater than or equal to 95%, greater than or equal to 98%, greater than or equal to 99%, greater than or equal to 99.5%, greater than or equal to 99.8%, greater than or equal to 99.9%, or greater than or equal to 99.99%.
- the final E1 efficiency of the filter media is less than or equal to 100%, less than or equal to 99.99%, less than or equal to 99.9%, less than or equal to 99.8%, less than or equal to 99.5%, less than or equal to 99%, less than or equal to 98%, less than or equal to 95%, less than or equal to 90%, less than or equal to 80%, less than or equal to 70%, less than or equal to 60%, less than or equal to 50%, or less than or equal to 40%. Combinations of the above-referenced ranges are also possible (e.g., a final E1 efficiency of greater than or equal to 36% and less than or equal to 100%, greater than or equal to 36% and less than or equal to 90%). Other ranges are also possible.
- the ASHRAE 52.2 test used herein involves a test air flow rate of 295 feet per minute (FPM) where the final pressure drop when the efficiency is measured is 1.5 inches of H 2 O on a column.
- the test is run at an air temperature of 20° C., a relative humidity of 40%, and a barometric pressure of 29.30 in Hg.
- Test conditions needs to be modified slightly as below.
- the testing uses a challenge aerosol of atomized KCl particles having a range of particle sizes between 0.3-1.0 microns (for determining E1 final efficiency), 1.0-3.0 microns (for determining E2 final efficiency), and/or 3.0-10.0 microns (for determining E3 final efficiency).
- the final E1 efficiency is determined by calculating the average minimum particle size efficiency for four ranges of particle sizes within the 0.3-1.0 micron particle size range: 0.3-0.4 micron particle size, 0.4-0.55 micron particle size, 0.55-0.7 micron particle size, 0.7-1.0 micron particle size, i.e., according to the following equation:
- Final E1 efficiency [(minPSE@(0.3-0.4 micron particle size)+minPSE@(0.4-0.55 micron particle size)+minPSE@(0.55-0.7 micron particle size)+minPSE@(0.7-1.0 micron particle size)]/4, where minPSE@(x-y micron particle size) is the minimum particle size efficiency for particles having a given x-y micron particle size range (e.g., 0.3-0.4 micron particle size particles).
- PSE Particle size efficiency
- a filter media described herein may have a particular final E2 efficiency (e.g., a final E2 efficiency of greater than or equal to 80%), according to the ASHRAE 52.2 standard.
- the final E2 efficiency of the filter media is greater than or equal to 80%, greater than or equal to 90%, greater than or equal to 95%, greater than or equal to 98%, greater than or equal to 99%, greater than or equal to 99.5%, or greater than or equal to 99.8%.
- the final E2 efficiency of the filter media is less than or equal to 99.9%, less than or equal to 99.8%, less than or equal to 99.5%, less than or equal to 99%, less than or equal to 98%, less than or equal to 95%, or less than or equal to 90%. Combinations of the above-referenced ranges are also possible (e.g., a final E2 efficiency of greater than or equal to 80% and less than or equal to 100%, greater than or equal to 80% and less than or equal to 90%). Other ranges are also possible.
- a filter media described herein may have a particular final E3 efficiency (e.g., a final E3 efficiency of greater than or equal to 90%), according to the ASHRAE 52.2 standard.
- the final E3 efficiency of the filter media is greater than or equal to 90%, greater than or equal to 95%, greater than or equal to 98%, greater than or equal to 99%, greater than or equal to 99.5%, or greater than or equal to 99.8%.
- the final E3 efficiency of the filter media is less than or equal to 99.9%, less than or equal to 99.8%, less than or equal to 99.5%, less than or equal to 99%, less than or equal to 98%, or less than or equal to 95%. Combinations of the above-referenced ranges are also possible (e.g., a final E3 efficiency of greater than or equal to 90% and less than or equal to 100%). Other ranges are also possible.
- the filter media may have a ratio of the value of thickness over instantaneous resistance of the second layer to the value of thickness over instantaneous resistance of the first layer of less than or equal to 20, less than or equal to 15, less than or equal to 10, less than or equal to 5, less than or equal to 3, less than or equal to 2, or less than or equal to 1.
- the filter media may have a ratio of the value of thickness over instantaneous resistance of the second layer to the value of thickness over instantaneous resistance of the first layer of greater than or equal to 0.5, greater than or equal to 1, greater than or equal to 2, greater than or equal to 3, greater than or equal to 5, greater than or equal to 10, or greater than or equal to 15.
- the value of the thickness over instantaneous resistance of the second layer is greater than the value of the thickness over instantaneous resistance of the first layer (e.g., such that the ratio of the value of thickness over instantaneous resistance of the second layer to the value of thickness over instantaneous resistance of the first layer is greater than 1).
- Combinations of the above-referenced ranges are also possible (e.g., greater than or equal to 0.5 and less than or equal to 20, greater than or equal to 1 and less than or equal to 10). Other ranges are also possible.
- a filter media described herein passes a P95 filter media test performed according to the NIOSH P-95 standard (NIOSH TEB-APR-STP-0053 (Revision 2.0)). Briefly, for a filter media to pass a P95 test, the maximum penetration during 200 mg loading of DOP should not exceed 5%, and the bandwidth of the filter media, defined as the penetration difference at 26 minutes and 30 minutes of the penetration test, should not exceed 0.1%. Maximum penetration and bandwidth are described in more detail below.
- the filter media having a TRF ratio within one or more ranges described above may pass a P95 test.
- the filter media having a TRF ratio within one or more ranges described above may pass a P99 test or a P100 test as described herein.
- a filter media described herein passes a P99 filter media test performed according to the NIOSH P-99 standard (NIOSH TEB-APR-STP-0052 (Revision 2.0)). Briefly, for a filter media to pass a P99 test, the maximum penetration during 200 mg loading of DOP should not exceed 1% and the bandwidth of the filter media, defined as the penetration difference at 26 minutes and 30 minutes of the penetration test, should not exceed 0.023%.
- the filter media comprising a first layer and a second layer passes a P100 filter media test performed according to the NIOSH P-100 standard (NIOSH TEB-APR-STP-0051 (Revision 2.0)). Briefly, for a filter media to pass a P100 test, the maximum penetration during 200 mg loading of DOP should not exceed 0.03% and the bandwidth of the filter media, defined as the penetration difference at 26 minutes and 30 minutes, should not exceed 0.004%.
- a filter media may have a ratio of the value of thickness over instantaneous resistance of the second layer to the value of thickness over instantaneous resistance of the first layer of less than or equal to 50, less than or equal to 40, less than or equal to 30, less than or equal to 20, less than or equal to 15, less than or equal to 10, less than or equal to 5, less than or equal to 3, less than or equal to 2, or less than or equal to 1.
- the filter media may have a ratio of the value of thickness over instantaneous resistance of the second layer to the value of thickness over instantaneous resistance of the first layer of greater than or equal to 0.5, greater than or equal to 1, greater than or equal to 2, greater than or equal to 3, greater than or equal to 5, greater than or equal to 10, greater than or equal to 15, greater than or equal to 20, greater than or equal to 30, or greater than or equal to 40. Combinations of the above-referenced ranges are also possible (e.g., greater than or equal to 0.5 and less than or equal to 50, greater than or equal to 1 and less than or equal to 30). Other ranges are also possible.
- the filter media having a TRF ratio within one or more ranges described above may pass a P99 test or a P100 test; however, other configurations are also possible.
- a filter media comprises a first layer comprising a plurality of fibers and a second layer adjacent the first layer.
- the first layer comprises a fluorinated species.
- the first layer has a first value of a thickness over instantaneous resistance of the first layer
- the second layer has a second value of a thickness over instantaneous resistance of the second layer
- the ratio of the second value to the first value is less than or equal to 20.
- the filter media has an initial efficiency of greater than or equal to 95%.
- a filter media comprises a first layer (e.g., a meltblown layer) comprising a plurality of meltblown fibers and a fluorinated species (e.g., a fluorinated species having the formula —C n F 2n+1 , —C n F m , or C n F m —(C x H y )—Z, where n is an integer equal or greater than 1 and less than or equal to 11, m is an integer equal or greater than 1 and less than or equal to 14, x is an integer greater than 0 and less than or equal to 12, y is an integer greater than 0 and less than or equal to 25, and Z is an end functional group that can be selected from the group consisting of acrylate, methacrylate, alcohol, aldehyde, carboxylic acid, olefins, silane, bromide, iodide, thiol, amine, phenol, isocyanate, sulfonate, e
- the fluorinated species may be deposited onto/into the first layer by a CVD deposition process or another suitable process.
- the filter media also includes a second layer directly adjacent the first layer.
- the second layer comprises a first plurality of fibers (e.g., synthetic fibers such as dry spun acrylic fibers) and a second plurality fibers (e.g., synthetic fibers such as polypropylene fibers).
- the second layer is a charged layer.
- Other materials for the first and/or second plurality of fibers may also be used (e.g., two fibers that have a certain difference in dielectric constant as described herein).
- the first polymer and the second polymer have a difference in dielectric constants of at least about 0.8.
- a filter media comprises a first layer comprising at least three meltblown sublayers, each sublayer comprising a plurality of meltblown fibers and a fluorinated species (e.g., a fluorinated species having the formula —C n F 2n+1 , —C n F m , or C n F m —(C x H y )—Z, where n is an integer equal or greater than 1 and less than or equal to 11, m is an integer equal or greater than 1 and less than or equal to 14, x is an integer greater than 0 and less than or equal to 12, y is an integer greater than 0 and less than or equal to 25, and Z is an end functional group that can be selected from the group consisting of acrylate, methacrylate, alcohol, aldehyde, carboxylic acid, olefins, silane, bromide, iodide, thiol, amine, phenol, isocyanate, sulfonate,
- the filter media also includes a second layer directly adjacent the first layer, the second layer comprising at least two sublayers.
- Each sublayer may comprise a first plurality of fibers (e.g., synthetic fibers such as dry spun acrylic fibers) and a second plurality of fibers (e.g., synthetic fibers such as polypropylene fibers).
- Other materials for the first and/or second plurality of fibers may also be used (e.g., two fibers that have a certain difference in dielectric constant as described herein).
- the first polymer and the second polymer have a difference in dielectric constants of at least about 0.8.
- the second layer may be charged.
- a filter media comprises a first layer comprises at least two meltblown sublayers, each sublayer comprising a plurality of meltblown fibers and a fluorinated species (e.g., a fluorinated species having the formula —C n F 2n+1 , —C n F m , or C n F m —(C x H y )—Z, where n is an integer equal or greater than 1 and less than or equal to 11, m is an integer equal or greater than 1 and less than or equal to 14, x is an integer greater than 0 and less than or equal to 12, y is an integer greater than 0 and less than or equal to 25, and Z is an end functional group that can be selected from the group consisting of acrylate, methacrylate, alcohol, aldehyde, carboxylic acid, olefins, silane, bromide, iodide, thiol, amine, phenol, isocyanate, sulfonate,
- the second layer may comprise a first plurality of fibers (e.g., synthetic fibers) and a second plurality of fibers (e.g., synthetic fibers), wherein the first and second plurality of fibers are different.
- the first polymer and the second polymer have a difference in dielectric constants of at least about 0.8. The second layer may be charged.
- the filter media further comprises one or more support layers (e.g., a meltblown layer, a spunbond layer, a wet-laid layer, a dry-laid layer).
- filter media 100 comprises a first layer 110 , a second layer 120 , and a support layer 130 (e.g., a third layer).
- the first layer may be adjacent the second layer, although other configurations are also possible.
- the support layer e.g., the third layer
- the support layer may be adjacent the second layer or disposed between the first layer and the second layer.
- the support layer may be attached to the first layer to provide support for the first layer, and/or may be attached to the second layer to provide support for the second layer.
- a support layer is positioned between the first layer and the second layer.
- the second layer e.g., a charged layer
- the support layer e.g., a third layer
- the second layer e.g., a charged layer
- the support layer e.g., a third layer
- the second layer (e.g., a charged layer) is upstream of the first layer (e.g., a non-wet laid layer) and the support layer (e.g., a third layer) is adjacent to and upstream of the second layer.
- the second layer e.g., a charged layer
- the first layer e.g., a non-wet laid layer
- the support layer e.g., a third layer
- the second layer e.g., a charged layer
- the first layer e.g., a third layer
- the support layer e.g., a third layer
- Such a support layer is a separate layer and is not included in the calculation of the value of thickness over instantaneous resistance for the first layer or the second layer, nor included into the calculation of the values of basis weight over air permeability for the first layer or the second layer.
- the support layer(s) may be formed of a different fiber type (including a different fiber composition/materials) than fibers of the first layer and/or fibers of second layer.
- the one or more support layers comprise a plurality of spunbond fibers, wetlaid fibers, drylaid fibers and/or meltblown fibers.
- the support layer e.g., spunbond layer
- the support layer may be coated (e.g., with a fluorinated species) as described herein.
- the support layer e.g., spunbond layer
- the support layer may be needled to the second layer.
- the support layer aids in fabrication and/or manipulation of the layer(s), but is removed from the first and/or second layer prior to incorporation of the layer(s) into a filter media and/or a filter element.
- the support layer(s) may be present in the final filter media and/or a filter element.
- the support layer comprises a plurality of fibers comprising a polymer.
- suitable polymers for the support layer include polypropylene, high density polyethylene, low density polyethylene, linear low density polyethylene, ethylene-vinyl acetate, polyamide, polyurethane, polyethylene terephthalate, polylactic acid, and copolymers thereof.
- a single fiber composition is used to form the support layer.
- the support layer may be designed to have a particular air permeability.
- the air permeability of the support layer is greater than or equal to 1100 CFM, greater than or equal to 1500 CFM, greater than or equal to 2000 CFM, greater than or equal to 3000 CFM, greater than or equal to 4000 CFM, greater than or equal to 5000 CFM, greater than or equal to 6000 CFM, greater than or equal to 7000 CFM, greater than or equal to 8000 CFM, or greater than or equal to 9000 CFM.
- the air permeability of the support layer is less than or equal to 10000 CFM, less than or equal to 9000 CFM, less than or equal to 8000 CFM, less than or equal to 7000 CFM, less than or equal to 6000 CFM, less than or equal to 5000 CFM, less than or equal to 4000 CFM, less than or equal to 3000 CFM, less than or equal to 2000, or less than or equal to 1500 CFM. Combinations of the above referenced ranges are also possible (e.g., greater than or equal to 1100 CFM and less than or equal to 10000 CFM). Other ranges are also possible.
- the support layer may have a particular basis weight.
- the basis weight of the support layer may be greater than or equal to 0.5 g/m 2 , greater than or equal to 1 g/m 2 , greater than or equal to 2 g/m 2 , greater than or equal to 5 g/m 2 , greater than or equal to 10 g/m 2 , greater than or equal to 20 g/m 2 , greater than or equal to 50 g/m 2 , or greater than or equal to 100 g/m 2 .
- the basis weight of the support layer is less than or equal to 150 g/m 2 , less than or equal to 100 g/m 2 , less than or equal to 50 g/m 2 , less than or equal to 20 g/m 2 , less than or equal to 10 g/m 2 , less than or equal to 5 g/m 2 , less than or equal to 2 g/m 2 , or less than or equal to 1 g/m 2 . Combinations of the above-referenced ranges are also possible (e.g., greater than or equal to 0.5 g/m 2 and less than or equal to 150 g/m 2 , greater than or equal to 2 g/m 2 and less than or equal to 50 g/m 2 ). Other ranges are also possible.
- a filter media comprises a first layer comprising a plurality of fibers and a second layer adjacent the first layer.
- the first layer and the second layer may be mated to one another using various techniques in the art.
- the first layer and the second layer may be mated by needling.
- the filter media further comprises a support layer (e.g., a third layer)
- the first layer, second layer, and support layer may be mated to one another by needling.
- the filter media does not comprise an adhesive and/or an adhesive layer, or is substantially free of adhesive.
- the filter media may have a particular needle density (e.g., greater than or equal to 10 needle punches per square inch (PPSI)).
- PPSI needle punches per square inch
- the needle density of the filter media is between 10 PPSI and 30 PPSI.
- the needle density of the filter media is greater than or equal to 10 PPSI, greater than or equal to 12 PPSI, greater than or equal to 15 PPSI, greater than or equal to 17 PPSI, greater than or equal to 20 PPSI, or greater than or equal to 25 PPSI.
- the needle density of the filter media is less than or equal to 30 PPSI, less than or equal to 25 PPSI, less than or equal to 20 PPSI, less than or equal to 17 PPSI, less than or equal to 15 PPSI, or less than or equal to 12 PPSI. Combinations of the above referenced ranges are also possible (e.g., greater than or equal to 10 PPSI and less than or equal to 30 PPSI). Other ranges are also possible.
- a filter media comprises a first layer comprising a plurality of fibers and a second layer adjacent the first layer.
- the first layer has a first value of a thickness over instantaneous resistance of the first layer
- the second layer has a second value of a thickness over instantaneous resistance of the second layer
- the ratio of the second value to the first value is less than or equal to 20.
- the filter media has an initial efficiency of greater than or equal to 95%.
- a filter media comprises a first layer comprising a plurality of fibers and a second layer.
- the first layer is adjacent the second layer.
- the second layer is charged.
- the first layer has a first value of a basis weight over air permeability of the first layer
- the second layer has a second value of a basis weight over air permeability of the second layer
- the ratio of the first value to the second value is less than or equal to 5 (e.g., less than or equal to 4).
- the filter media has an final E1 efficiency of greater than or equal to 36%.
- such a media has a first layer having a basis weight of less than or equal to 20 g/m 2 and a plurality of fibers having an average fiber diameter of greater than or equal to 1 micron and less than or equal to 8 microns.
- the second layer has a basis weight of greater than or equal to 30 g/m 2 and less than or equal to 85 g/m 2 .
- the filter media having the WOA ratio of less than or equal to 5 has an initial resistance of less than or equal to 1.6 mm H 2 O (or another suitable range described herein).
- the first layer may have air permeability of greater than or equal to 200 CFM and less than or equal to 650 CFM.
- the first layer may comprise two or more sublayers and/or may be a non-wet laid layer.
- the first layer comprises a plurality of meltblown fibers, meltspun fibers, melt electrospun fibers, solvent electrospun fibers, centrifugal spun fibers, spunbond fibers, and/or combinations thereof.
- the second layer has an air permeability of greater than or equal to 330 CFM and less than or equal to 1000 CFM.
- the second layer may comprise two or more sublayers and/or may comprise a first plurality of fibers comprising a first polymer and a second plurality of fibers comprising a second polymer (wherein the first and second polymers are different).
- the first polymer may comprise acrylic (e.g., dry spun acrylic) and the second polymer may comprise polypropylene.
- the second layer may be positioned upstream relative to the first layer or in any other suitable configuration described herein.
- the filter media comprises a support layer having an air permeability of greater than or equal to 1100 CFM and less than or equal to 10000 CFM.
- the filter media may be needled and/or does not comprise an adhesive or adhesive layer, or is substantially free of adhesive.
- the filter media may have a final E1 efficiency of greater than or equal to 36%, according to the ASHRAE 52.2 standard described herein.
- a filter element comprises a filter media described herein.
- Such filter elements may be used, for example, in an HVAC filter.
- the first layer does not include a fluorinated species and is not charged.
- the first layer may include a fluorinated species as described herein.
- the first layer has a value of basis weight over air permeability of the first layer of greater than or equal to 0.000125 g/m 2 CFM and less than or equal to 0.2 g/m 2 CFM (or another suitable range described herein), and the second layer has a value of basis weight over air permeability of the second layer of greater than or equal to 0.03 g/m 2 CFM and less than or equal to 0.25 g/m 2 CFM (or another suitable range described herein).
- the first layer has a first value of a basis weight over air permeability of the first layer and the second layer has a second value of a basis weight over air permeability of the second layer, such that the ratio of the first value to the second value is less than or equal to 5 (or another suitable range described herein, e.g., less than or equal to 4).
- the first layer has a value of thickness over instantaneous resistance of the first layer of greater than or equal to 2 mils/mmH 2 O and less than or equal to 50 mils/mm H 2 O (or another suitable range described herein)
- the second layer has a value of thickness over instantaneous resistance of the second layer of greater than or equal to 20 mils/mmH 2 O and less than or equal to 150 mils/mm H 2 O (or another suitable range described herein).
- the first layer has a first value of a thickness over instantaneous resistance of the first layer and the second layer has a second value of a thickness over instantaneous resistance of the second layer, such that the ratio of the second value to the first value is less than or equal to 20 (or another suitable range described herein).
- the basis weight of the first layer is greater than or equal to 0.1 g/m 2 and less than or equal to 500 g/m 2 (e.g., greater than or equal to 6 g/m 2 and less than or equal to 80 g/m 2 ) and/or the basis weight of the second layer is greater than or equal to 20 g/m 2 and less than or equal to 600 g/m 2 (e.g., greater than or equal to 50 g/m 2 and less than or equal to 200 g/m 2 ).
- the basis weight of the first layer is less than or equal to 20 g/m 2 and/or the basis weight of the second layer is greater than or equal to 30 g/m 2 and less than or equal to 85 g/m 2 .
- the first plurality of fibers comprises a first polymer and the second plurality of fibers comprises a second polymer where the first polymer and the second polymer have a difference in dielectric constants of at least about 0.8.
- the filter media may be designed to have a particular ratio of the solidity of the first layer to the solidity of the second layer.
- the ratio of the solidity of the first layer to the solidity of the second layer is greater than or equal to 0.1, greater than or equal to 0.5, greater than or equal to 1, greater than or equal to 2, greater than or equal to 5, greater than or equal to 10, or greater than or equal to 20.
- the ratio of the solidity of the first layer to the solidity of the second layer may be less than or equal to 25, less than or equal to 20, less than or equal to 10, less than or equal to 5, less than or equal to 2, less than or equal to 1, or less than or equal to 0.5. Combinations of the above-referenced ranges are also possible (e.g., greater than or equal to 0.1 and less than or equal to 25, greater than or equal to 1 and less than or equal to 5). Other ranges are also possible.
- the total thickness of the filter media may be greater than or equal to 30 mils, greater than or equal to 40 mils, greater than or equal to 50 mils, greater than or equal to 75 mils, greater than or equal to 100 mils, greater than or equal to 150 mils, greater than or equal to 200 mils, greater than or equal to 250 mils, greater than or equal to 300 mils, greater than or equal to 500 mils, or greater than or equal to 750 mils.
- the total thickness of the filter media is less than or equal to 1000 mils, less than or equal to 750 mils, less than or equal to 500 mils, less than or equal to 300 mils, less than or equal to 250 mils, less than or equal to 200 mils, less than or equal to 150 mils, less than or equal to 100 mils, less than or equal to 75 mils, less than or equal to 50 mils, or less than or equal to 40 mils. Combinations of the above-referenced ranges are also possible (e.g., greater than or equal to 30 mils and less than or equal to 1000 mils, greater than or equal to 30 mils and less than or equal to 300 mils, greater than or equal to 50 mils and less than or equal to 200 mils).
- Total thickness is measured using a Federal C&R thickness gauge according to the standard ASTM D1778. Briefly, the gauge has 1 square inch area in contact with the filter media and uses a 2 ounce load to lightly compress the sample as follows: the gauge is zeroed first without the filter media, then raised to allow enough space to insert the filter media, then lowered again to rest on the filter media without impact. The total thickness is noted on the dial.
- a filter media and/or a layer may be designed to have a particular resistance (e.g., instantaneous resistance, initial resistance), penetration (e.g., instantaneous penetration, initial penetration, maximum penetration, bandwidth) or efficiency (e.g., instantaneous efficiency, initial efficiency). Resistance, penetration and efficiency are measured using a 8130 CertiTestTM automated filter testing unit from TSI, Inc. equipped with a DiOctyl Phthalate (DOP) generator for DOP aerosol testing based on the NIOSH P-series standard (e.g., NIOSH TEB-APR-STP-0053 (Revision 2.0)) for DOP particles.
- DOP DiOctyl Phthalate
- the particle size created by the DOP particle generator is 0.3 microns (mass mean diameter).
- the test involves using a DOP particle concentration in an air stream of about 125 mg/m 3 , for a continuous 30 minute challenge to accumulate 200 mg loading at a face velocity 16.4 FPM over a 100 cm 2 face area of the filter media/layer.
- Initial resistance, initial penetration, and initial efficiency are determined at 1 minute after starting the test.
- Maximum penetration corresponds to the maximum penetration measurement during the 30 minute test. Bandwidth is calculated by taking the percentage difference in penetration between measurements obtained at 26 minutes and 30 minutes of the test.
- the filter media comprising a first layer and a second layer as described herein may have lower initial resistance compared to certain existing filter media.
- the initial resistance of a filter media described herein is less than or equal to 35 mm H 2 O, less than or equal to 30 mm H 2 O, less than or equal to 25 mm H 2 O, less than or equal to 20 mm H 2 O, less than or equal to 15 mm H 2 O, less than or equal to 10 mm H 2 O, less than or equal to 9, less than or equal to 8 mm H 2 O, less than or equal to 5 mm H 2 O, less than or equal to 4 mm H 2 O, less than or equal to 3 mmH 2 O, less than or equal to 2 mm H 2 O, less than or equal to 1.6 mm H 2 O, less than or equal to 1 mm H 2 O, less than or equal to 0.5 mm H 2 O, less than or equal to 0.1 mm H 2 O, or less than or equal to 0.05 mm H 2 O.
- the initial resistance of the filter media is greater than or equal to 0.01 mm H 2 O, greater than or equal to 0.05 mm H 2 O, greater than or equal to 0.1 mm H 2 O, greater than or equal to 0.5 mm H 2 O, greater than or equal to 1 mm H 2 O, greater than or equal to 1.6 mm H 2 O, greater than or equal to 2 mm H 2 O, greater than or equal to 4 mm H 2 O, greater than or equal to 5 mm H 2 O, greater than or equal to 10 mm H 2 O, greater than or equal to 15 mm H 2 O, greater than or equal to 20 mm H 2 O, greater than or equal to 25 mm H 2 O, or greater than or equal to 30 mm H 2 O.
- the filter media (e.g., a filter media that passes a P95 test as described herein) comprising a first layer and a second layer as described herein has an initial resistance of less than 1.6 mm H 2 O.
- the filter media and/or layer may have a particular efficiency and/or penetration.
- the instantaneous efficiency of the filter media is greater than or equal to 90%, greater than or equal to 92%, greater than or equal to 95%, greater than or equal to 96%, greater than or equal to 97%, greater than or equal to 98%, greater than or equal to 99%, greater than or equal to 99.5%, greater than or equal to 99.8%, greater than or equal to 99.9%, or greater than or equal to 99.99%.
- the instantaneous efficiency of the filter media is less than or equal to 100%, less than or equal to 99.99%, less than or equal to 99.9%, less than or equal to 99.8%, less than or equal to 99.5%, less than or equal to 99%, less than or equal to 98%, less than or equal to 97%, less than or equal to 96%, less than or equal to 95%, or less than or equal to 92%. Combinations of the above-referenced ranges are also possible (e.g., an instantaneous efficiency of greater than or equal to 90% and less than or equal to 100%, greater than or equal to 95% and less than or equal to 100%). Other ranges are also possible.
- the initial efficiency of the filter media is greater than or equal to 90%, greater than or equal to 92%, greater than or equal to 95%, greater than or equal to 96%, greater than or equal to 97%, greater than or equal to 98%, greater than or equal to 99%, greater than or equal to 99.5%, greater than or equal to 99.8%, greater than or equal to 99.9%, or greater than or equal to 99.99%.
- the initial efficiency of the filter media is less than or equal to 100%, less than or equal to 99.99%, less than or equal to 99.9%, less than or equal to 99.8%, less than or equal to 99.5%, less than or equal to 99%, less than or equal to 98%, less than or equal to 97%, less than or equal to 96%, less than or equal to 95%, or less than or equal to 92%. Combinations of the above-referenced ranges are also possible (e.g., an initial efficiency of greater than or equal to 90% and less than or equal to 100%, greater than or equal to 95% and less than or equal to 100%). Other ranges are also possible.
- the filter media described herein may be designed to have a particular range of maximum penetration.
- the filter media described herein has a maximum penetration of less than or equal to 10%, less than or equal to 5%, less than or equal to 2%, less than or equal to 1%, less than or equal to 0.5%, or less than or equal to 0.1%.
- the filter media has a maximum penetration of greater than or equal to 0%, greater than or equal to 0.1%, greater than or equal to 0.5%, greater than or equal to 1%, greater than or equal to 2%, or greater than or equal to 5%. Combinations of the above-referenced ranges are also possible (e.g., greater than or equal to 0% and less than or equal to 10%, greater than or equal to 0% and less than or equal to 2%).
- the filter media described herein may have a bandwidth.
- the bandwidth gives an indication of stability of a filter media's efficiency during extended usage, wherein lower values of bandwidth indicate greater stability of the filter media's efficiency compared to higher values.
- the bandwidth of the filter media is less than or equal to 3%, less than or equal to 2%, less than or equal to 1%, less than or equal to 0.5%, less than or equal to 0.1%, less than or equal to 0.05%, less than or equal to 0.023%, less than or equal to 0.005%, or less than or equal to 0.004%.
- the bandwidth of the filter media is greater than or equal to 0%, greater than or equal to 0.004%, greater than or equal to 0.005%, greater than or equal to 0.023%, greater than or equal to 0.05%, greater than or equal to 0.1%, greater than or equal to 0.5%, greater than or equal to 1%, or greater than or equal to 2%. Combinations of the above-referenced ranges are also possible (e.g., less than or equal to 3% and greater than or equal to 0%, less than or equal to 0.1% and greater than or equal to 0.1%). Other ranges are also possible.
- the filter media described herein may be tailored to have a particular oil repellency level.
- Such filter media may be used, for example, to remove or coalesce oil, lubricants, and/or cooling agents from a gas stream that passes through the filter media.
- the oil repellency level of the filter media or layer or sublayer is between 1 and 7 (e.g., 1-4, 2-5, 3-6, 4-7).
- the oil repellency level of the filter media or layer or sublayer is 1, 2, 3, 4, 5, 6, or 7.
- Oil repellency level as described herein is determined according to AATCC TM 118 (1997) measured at 23° C.
- test oil having an average droplet diameter of about 2 mm
- the test oil with the greatest oil surface tension that does not wet e.g., has a contact angle greater than or equal to 90 degrees with the surface
- the surface of the filter media or layer or sublayer after 30 seconds of contact with the filter media at 23° C. and 50% RH corresponds to the oil repellency level (listed in Table 2).
- the filter media or layer or sublayer has an oil repellency level of 4.
- the filter media or layer or sublayer has an oil repellency level of 5.
- the filter media or layer or sublayer has an oil repellency level of 6.
- the oil repellency level is expressed to the nearest 0.5 value determined by subtracting 0.5 from the number of the test liquid.
- the filter media or layer or sublayer has an oil repellency level of 5.5.
- a layer of the filter media may be a non-wet laid layer formed using a non-wet laid process (e.g., an air laid process, a carding process, a meltblown process).
- a non-wet laid process e.g., an air laid process, a carding process, a meltblown process.
- an air laid process or a carding process may be used.
- fibers may be mixed while air is blown onto a conveyor.
- the fibers are manipulated by rollers and extensions (e.g., hooks, needles) associated with the rollers.
- a layer of the filter media may include fibers formed from a meltblown process.
- the meltblown layer may have one or more characteristics described in commonly-owned U.S. Pat. No. 8,608,817, entitled “Meltblown Filter Medium”, issued on Dec. 17, 2013, which is based on U.S. patent application Ser. No. 12/266,892 filed on May 14, 2009, commonly-owned U.S. Patent Publication No.
- 2012/0152824 entitled “Fine Fiber Filter Media and Processes”, which is based on patent application Ser. No. 12/971,539 filed on Dec. 17, 2010, commonly-owned U.S. Patent Publication No. 2012/0152824, entitled “Fine Fiber Milter Media and Processes”, which is based on patent application Ser. No. 12/971,539 filed on Dec. 17, 2010, and commonly-owned U.S. Patent Publication No. 2012/0152821, entitled “Fine Fiber Milter Media and Processes”, which is based on patent application Ser. No. 12/971,594 filed on Dec. 17, 2010, each of which is incorporated herein by reference in its entirety for all purposes.
- the filter media may be used for a number of applications, such as respirator and face mask applications, cabin air filtration, military garments, HVAC systems (e.g., for industrial areas and buildings), clean rooms, vacuum filtration, room air cleaning, and respirator protection equipment (e.g., industrial respirators).
- applications such as respirator and face mask applications, cabin air filtration, military garments, HVAC systems (e.g., for industrial areas and buildings), clean rooms, vacuum filtration, room air cleaning, and respirator protection equipment (e.g., industrial respirators).
- the filter media may be incorporated into a face mask.
- the filter media can be, for example, folded, edge sealed, collated, or molded, with or without a supporting structure, within the face mask.
- the face mask may be a full face piece or a half face piece, and may be disposable or reusable.
- face masks are used to protect the respiratory system when the air contains hazardous amounts of particulate contaminants in the form of solid particles or liquid droplets that can cause impairment through inhalation. Accordingly, a face mask generally needs to provide adequate protection with good breathability (e.g., low resistance).
- the face mask may be designed to filter dust, fog, fumes, vapors, smoke, sprays or mists.
- face masks may be worn in areas where activities such as grinding, welding, road paving (e.g., where hot asphalt fumes are present), coal mining, transferring diesel fuel, or pesticide spraying are performed.
- the face mask may also be designed for wearing in hospitals (e.g., performing surgery), distillers and refineries in chemical industries, painting facilities, or oil fields.
- the face mask may be a surgical face mask or an industrial face mask.
- the filter media may be incorporated into a variety of other suitable filter elements for use in various applications including gas filtration.
- the filter media may be used in heating and air conditioning ducts.
- Filter elements may have any suitable configuration as known in the art including bag filters and panel filters.
- Filter assemblies for filtration applications can include any of a variety of filter media and/or filter elements.
- the filter elements can include the above-described filter media and/or layers (e.g., first layer, second layer). Examples of filter elements include gas turbine filter elements, dust collector elements, heavy duty air filter elements, automotive air filter elements, air filter elements for large displacement gasoline engines (e.g., SUVs, pickup trucks, trucks), HVAC air filter elements, HEPA filter elements, ULPA filter elements, and vacuum bag filter elements.
- Filter elements can be incorporated into corresponding filter systems (gas turbine filter systems, heavy duty air filter systems, automotive air filter systems, HVAC air filter systems (including residential and industrial HVAC air filter systems), HEPA filter systems, ULPA filter system, and vacuum bag filter systems).
- the filter media can optionally be pleated into any of a variety of configurations (e.g., panel, cylindrical).
- Filter elements can also be in any suitable form, such as radial filter elements, panel filter elements, or channel flow elements.
- a radial filter element can include pleated filter media that are constrained within two open wire support materials in a cylindrical shape.
- the filter element includes a housing that may be disposed around the filter media.
- the housing can have various configurations, with the configurations varying based on the intended application.
- the housing may be formed of a frame that is disposed around the perimeter of the filter media.
- the frame may be thermally sealed around the perimeter.
- the frame has a generally rectangular configuration surrounding all four sides of a generally rectangular filter media.
- the frame may be formed from various materials, including for example, cardboard, metal, polymers, or any combination of suitable materials.
- the filter elements may also include a variety of other features known in the art, such as stabilizing features for stabilizing the filter media relative to the frame, spacers, or any other appropriate feature.
- the filter media can be incorporated into a bag (or pocket) filter element.
- a bag filter element may be formed by any suitable method, e.g., by placing two filter media together (or folding a single filter media in half), and mating three sides (or two if folded) to one another such that only one side remains open, thereby forming a pocket inside the filter.
- multiple filter pockets may be attached to a frame to form a filter element.
- the filter media and filter elements may have a variety of different constructions and the particular construction depends on the application in which the filter media and elements are used.
- a substrate may be added to the filter media.
- the filter elements may have the same property values as those noted above in connection with the filter media and/or layers.
- the above-noted instantaneous resistances, efficiencies, (total) thicknesses, and/or basis weight may also be found in filter elements.
- the filter media mechanically trap contaminant particles on the filter media as fluid (e.g., air) flows through the filter media.
- This example demonstrates the effects of the ratio of a value of thickness over instantaneous resistance of second layer to a value of thickness over instantaneous resistance of first layer on filter media performance.
- This example compares, for different filter media, the effects of a ratio of a value of a basis weight over air permeability of a first layer to a value of a basis weight over air permeability of a second layer and shows the resulting composite air permeability for the filter media.
- Samples were prepared as listed in Table 7:
- a first layer comprising a plurality of meltblown fibers (having a range of fiber diameters between 1 and 8 microns) was hand laid on a second, charged layer comprising 50 wt % dry spun acrylic and 50 wt % polypropylene polymer fibers, along with a support layer having an air permeability of greater than 1100 CFM.
- the first layer had a basis weight of less than 20 g/m 2 and the second layer had a basis weight between 30 g/m 2 and 85 g/m 2 .
- All three layers of filter media 1-6 were needled together in a single step, with a needle density of at least 10 needle punches per square inch. Filter media 7-10 were not needled together.
- the composite air permeability values listed in Table 7 for media 7-10 are the equivalent composite air permeability values for each filter media if media 7-10 were needled.
- the composite air permeability values for media 7-10 were calculated by first measuring the composite air permeability of the unneedled filter media, and then increasing the unneedled composite air permeability value by a calibration factor (in percent) derived from reference needled filter media of varying air permeabilities and basis weights.
- Filter media 1-10 did not include any adhesive nor any coating of a fluorinated species.
- Each of filter media 1-6 had a final E1 efficiency of greater than 36%, an initial resistance of less than 3 mm H 2 O, and a composite air permeability of greater than 200 CFM.
- Each of filter media 7-10 had a final E1 efficiency of greater than 36%, an initial resistance of greater than 5 mm H 2 O, and a composite air permeability of less than 200 CFM. Testing for E1 final efficiency of the filter media was performed according to the ASHRAE 52.2 standard described herein.
- FIG. 7 shows, for filter media 1-10, the air permeability of the filter media versus the ratio of the value of basis weight over air permeability of the first layer to the value of basis weight over air permeability of the second layer.
- a reference to “A and/or B,” when used in conjunction with open-ended language such as “comprising” can refer, in some embodiments, to A without B (optionally including elements other than B); in another embodiment, to B without A (optionally including elements other than A); in yet another embodiment, to both A and B (optionally including other elements); etc.
- the phrase “at least one,” in reference to a list of one or more elements, should be understood to mean at least one element selected from any one or more of the elements in the list of elements, but not necessarily including at least one of each and every element specifically listed within the list of elements and not excluding any combinations of elements in the list of elements.
- This definition also allows that elements may optionally be present other than the elements specifically identified within the list of elements to which the phrase “at least one” refers, whether related or unrelated to those elements specifically identified.
- “at least one of A and B” can refer, in some embodiments, to at least one, optionally including more than one, A, with no B present (and optionally including elements other than B); in another embodiment, to at least one, optionally including more than one, B, with no A present (and optionally including elements other than A); in yet another embodiment, to at least one, optionally including more than one, A, and at least one, optionally including more than one, B (and optionally including other elements); etc.
- alkane is given its ordinary meaning in the art and refers to a saturated hydrocarbon molecule.
- amine is given its ordinary meaning in the art and refers to a primary (—NH 2 ), secondary (—NHR x ), tertiary (—NR x R y ), or quaternary (—N + R x R y R z ) amine (e.g., where R x , R y , and R z are independently an aliphatic, alicyclic, alkyl, aryl, or other moieties, as defined herein).
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Filtering Materials (AREA)
- Laminated Bodies (AREA)
Abstract
Description
| TABLE 1 | |||
| Materials | Dielectric constant | ||
| Polytetrafluoroethylene | 2.10 | ||
| Polypropylene | 2.2-2.36 | ||
| Polyethylene | 2.25-2.35 | ||
| Polystyrene | 2.45-2.65 | ||
| Polyvinyl chloride | 2.8-3.1 | ||
| Polysulfone | 3.07 | ||
| Polyethersulfone | 3.10 | ||
| Polyethylene terephthalate | 3.1 | ||
| Polycarbonate | 3.17 | ||
| Acrylic | 3.5-4.5 | ||
| Paper | 3.85 | ||
| Nylon 6/6 | 4.0-4.6 | ||
| Polyurethane | 6.3 | ||
| Phenolic | 6.5 | ||
| Polyvinylidene fluoride | 8.4 | ||
Final E1 efficiency=[(minPSE@(0.3-0.4 micron particle size)+minPSE@(0.4-0.55 micron particle size)+minPSE@(0.55-0.7 micron particle size)+minPSE@(0.7-1.0 micron particle size)]/4,
where minPSE@(x-y micron particle size) is the minimum particle size efficiency for particles having a given x-y micron particle size range (e.g., 0.3-0.4 micron particle size particles).
PSE=(1−(downstream particle concentration/upstream particle concentration))*100.
Final E2 efficiency=[(minPSE@(1.0-1.3 micron particle size)+minPSE@(1.3-1.6 micron particle size)+minPSE@(1.6-2.2 micron particle size)+minPSE@(2.2-3.0 micron particle size)]/4,
where minPSE@(x-y micron particle size) is the minimum particle size efficiency for particles having a given x-y micron particle size range (e.g., 1.0-3.0 micron particle size particles).
Final E3 efficiency=[(minPSE@(3.0-4.0 micron particle size)+minPSE@(4.0-5.5 micron particle size)+minPSE@(5.5-7.0 micron particle size)+minPSE@(7.0-10.0 micron particle size)]/4,
where minPSE@(x-y micron particle size) is the minimum particle size efficiency for particles having a given x-y micron particle size range (e.g., 3.0-10.0 micron particle size particles).
| TABLE 2 | ||
| Oil Repellency | Surface tension | |
| Level | Test Oil | (in mN/m) |
| 1 | Kaydol (mineral oil) | 31 |
| 2 | 65/35 Kaydol/n-hexadecane | 28 |
| 3 | n-hexadecane | 27.5 |
| 4 | n-tetradecane | 26.6 |
| 5 | n-dodecane | 25.4 |
| 6 | n-decane | 23.8 |
| 7 | n-octane | 21.6 |
| 8 | n-heptane | 20.1 |
| TABLE 3 | ||
| Filter | ||
| Media | 1st Layer with fluorinated species | 2nd Layer |
| 1 | 3 sublayers B | 2 sublayers C50 |
| 2* | 1 sublayer C + 2 sublayers D | 2 sublayers C50 |
| 3 | 2 sublayers D | 2 sublayers C100 |
| 4 | 1 sublayer D + 1 sublayer E | 2 sublayers C100 |
| 5 | 1 sublayer E | 1 sublayer C200 |
| 6 | 3 sublayers F | 2 sublayers C100 |
| 7 | 2 sublayers F | 1 sublayer C200 |
| *Filter media includes fluorinated SB intervening layer between 1st and 2nd layers | ||
| SB = spunbond, light weight nonwoven polypropylene fiber material as structure reinforcement | ||
| B = a meltblown polypropylene fiber layer with basis weight of 20 g/m2 reinforced by a SB layer | ||
| C = a fine fiber meltblown polypropylene fiber layer with basis weight of 6 g/m2 reinforced by a SB layer | ||
| D = a meltblown polypropylene fiber layer with basis weight of 20 g/m2 | ||
| E = a meltblown polypropylene fiber layer with basis weight of 20 g/m2 reinforced by a SB layer | ||
| F = a meltblown polypropylene layer with basis weight of 80 g/m2 | ||
| C50, C100, C200 = a charged layer made of polypropylene and acrylic fibers of 50, 100, 200 g/m2 basis weight, respectively | ||
Tables 4-5 summarize the various properties of the filter media listed in Table 3. Table 4 summarizes the instantaneous resistance, instantaneous penetration, basis weight, uncompressed thickness, and solidity for the first layer of each filter media listed in Table 3.
| TABLE 4 | ||
| 1st layer | ||
| Uncompressed | ||||||
| Mitutoya Un- | thickness to | |||||
| Instantaneous | Basis | compressed | instantaneous | |||
| Filter | Resistance | Instantaneous | weight, | Thickness, | resistance ratio of the | |
| Media | (in mm H2O) | Penetration | gsm | mil | Solidity | 1st layer (TRF) |
| 1 | 13.2 | 2.46% | 75 | 46 | 0.082 | 3.5 |
| 2 | 13.5 | 2.17% | 76 | 48 | 0.074 | 3.5 |
| 3 | 8 | 1.28% | 40 | 24 | 0.085 | 3.1 |
| 4 | 8.3 | 1.19% | 55 | 34 | 0.081 | 4.1 |
| 5 | 4 | 11% | 35 | 22 | 0.078 | 5.5 |
| 6 | 5.7 | 1.60% | 240 | 162 | 0.071 | 28.5 |
| 7 | 4.4 | 6.38% | 160 | 108 | 0.071 | 24.6 |
Table 5 summarizes the instantaneous resistance, instantaneous penetration, basis weight, uncompressed thickness, and solidity for the second layer of each filter media listed in Table 3.
| TABLE 5 | ||
| 2nd Layer | ||
| Un-compressed | ||||||
| Mitutoya Un- | thickness to | |||||
| Instantaneous | Basis | compressed | instantaneous | |||
| Filter | Resistance | Instantaneous | weight, | Thickness, | resistance ratio of the | |
| Media | (in mm H2O) | Penetration | gsm | mil | Solidity | 2nd layer (TRF) |
| 1 | 1.2 | 15.20% | 100 | 152 | 0.033 | 127 |
| 2 | 1.2 | 15.20% | 100 | 152 | 0.033 | 127 |
| 3 | 2 | 1.77% | 200 | 230 | 0.037 | 115 |
| 4 | 2 | 1.77% | 200 | 230 | 0.037 | 115 |
| 5 | 2.3 | 0.58% | 200 | 132 | 0.064 | 57 |
| 6 | 2 | 1.77% | 200 | 230 | 0.037 | 115 |
| 7 | 2.3 | 0.58% | 200 | 132 | 0.064 | 57 |
Table 6 summarizes the total thickness, initial resistance, initial penetration, and the ratio of a value of thickness over instantaneous resistance of the second layer to a value of thickness over instantaneous resistance of first layer (TRF ratio), of the filter media listed in Table 3. As shown in Table 6, which is plotted in
| TABLE 6 | ||||
| Ratio of the value of thickness over | ||||
| Total | Initial | instantaneous resistance of second | ||
| Filter | Thickness, | Resistance, | Initial | layer to the value of thickness over |
| Media | mil* | mm H2O | penetration | instantaneous resistance of first layer |
| 1 | 136 | 14.4 | 0.37% | 36 |
| 2 | 140 | 14.7 | 0.33% | 36 |
| 3 | 189 | 10.1 | 0.05% | 38 |
| 4 | 200 | 11.3 | 0.04% | 28 |
| 5 | 142 | 7 | 0.04% | 10 |
| 6 | 290 | 7.7 | 0.31% | 4 |
| 7 | 194 | 6.5 | 0.22% | 2 |
| *Measured according to the standard ASTM D1778. | ||||
| TABLE 7 | ||
| Total Basis Weight | ||
| Filter | (first and second layers), | Composite |
| Media | g/m2 | Air perm, CFM |
| 1 | 67 | 384 |
| 2 | 65 | 350 |
| 3 | 68 | 278 |
| 4 | 66 | 201 |
| 5 | 81 | 207 |
| 6 | 65 | 280 |
| 7 | 80 | 72 |
| 8 | 88 | 64 |
| 9 | 98 | 57 |
| 10 | 108 | 83 |
Claims (21)
Priority Applications (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US15/217,718 US12420221B2 (en) | 2016-07-01 | 2016-07-22 | Multi-layered electret-containing filtration media |
| PCT/US2017/043249 WO2018017937A1 (en) | 2016-07-22 | 2017-07-21 | Multi-layered electret-containing filtration media |
| CN201780044830.6A CN109475798A (en) | 2016-07-22 | 2017-07-21 | Multilayer electret-containing filter media |
| EP17831940.6A EP3487602A4 (en) | 2016-07-22 | 2017-07-21 | MULTI-LAYERED FILTRATION MEDIA CONTAINING ELECTRETS |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US15/200,612 US20180001244A1 (en) | 2016-07-01 | 2016-07-01 | Multi-layered electret-containing filtration media |
| US15/217,718 US12420221B2 (en) | 2016-07-01 | 2016-07-22 | Multi-layered electret-containing filtration media |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US15/200,612 Continuation-In-Part US20180001244A1 (en) | 2016-07-01 | 2016-07-01 | Multi-layered electret-containing filtration media |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| US20180001247A1 US20180001247A1 (en) | 2018-01-04 |
| US12420221B2 true US12420221B2 (en) | 2025-09-23 |
Family
ID=60806479
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US15/217,718 Active US12420221B2 (en) | 2016-07-01 | 2016-07-22 | Multi-layered electret-containing filtration media |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US12420221B2 (en) |
Families Citing this family (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102016015248A1 (en) * | 2016-12-21 | 2018-06-21 | Johns Manville Europe Gmbh | Highly efficient filter medium |
| US10814261B2 (en) | 2017-02-21 | 2020-10-27 | Hollingsworth & Vose Company | Electret-containing filter media |
| US11077394B2 (en) | 2017-02-21 | 2021-08-03 | Hollingsworth & Vose Company | Electret-containing filter media |
| US10512862B2 (en) * | 2017-09-26 | 2019-12-24 | Veeco Instruments Inc. | Filter element for wafer processing assembly |
| US11433332B2 (en) * | 2018-11-05 | 2022-09-06 | Hollingsworth & Vose Company | Filter media with irregular structure |
| US11420143B2 (en) | 2018-11-05 | 2022-08-23 | Hollingsworth & Vose Company | Filter media with irregular structure and/or reversibly stretchable layers |
| CN114938636A (en) * | 2019-10-08 | 2022-08-23 | 唐纳森公司 | Filter media layer including mixed diameter fine fibers |
| US20210187421A1 (en) * | 2019-12-19 | 2021-06-24 | Hollingsworth & Vose Company | Filter media comprising a non-wetlaid backer |
| CN111229051A (en) * | 2020-03-12 | 2020-06-05 | 上海市纺织科学研究院有限公司 | Preparation method of electrostatic spinning polysulfonamide electret composite filter material |
| US20210370218A1 (en) * | 2020-05-29 | 2021-12-02 | Hollingsworth & Vose Company | Filter media comprising adsorptive particles |
| CA3268681A1 (en) * | 2022-09-28 | 2024-04-04 | Mativ Luxembourg | Filters with electrostatic filtering capabilities |
Citations (208)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US853981A (en) | 1906-05-29 | 1907-05-21 | George Kneuper | Filtering material. |
| US2196821A (en) | 1938-05-14 | 1940-04-09 | Motor Improvements Inc | Filter |
| US2208443A (en) * | 1938-04-06 | 1940-07-16 | Carrier Corp | Air conditioning method and apparatus |
| US2235005A (en) * | 1938-04-06 | 1941-03-18 | Carrier Corp | Air conditioning method |
| US2392901A (en) | 1943-03-20 | 1946-01-15 | Cleo E Brown | Filter |
| US2663156A (en) * | 1952-03-24 | 1953-12-22 | Jess F Baker | Apparatus for cooling and dehumidifying air |
| US2928765A (en) | 1957-02-11 | 1960-03-15 | C H Dexter & Sons Inc | Air filter paper and method of making same |
| US3353800A (en) * | 1965-01-11 | 1967-11-21 | Detrick M H Co | Apparatus for removing solids from hot gases |
| US3654851A (en) * | 1970-04-08 | 1972-04-11 | Mannie Bertin | Diffusers for conditioned air conduits |
| US3656882A (en) | 1970-03-09 | 1972-04-18 | Celanese Corp | ACRYLIC FIBER STABILIZATION CATALYZED BY Co(II) AND Ce(III) CATIONS |
| US3855133A (en) | 1971-12-28 | 1974-12-17 | Sartorius Membranfilter Gmbh | Multi-layer filter membrane |
| US3908528A (en) * | 1973-07-30 | 1975-09-30 | Mannie Bertin | Diffusers for conditioned air |
| US3944686A (en) | 1974-06-19 | 1976-03-16 | Pfizer Inc. | Method for vapor depositing pyrolytic carbon on porous sheets of carbon material |
| US4033881A (en) | 1975-01-06 | 1977-07-05 | Pall Corporation | Multilayer paper sheet filter cartridges |
| US4048953A (en) | 1974-06-19 | 1977-09-20 | Pfizer Inc. | Apparatus for vapor depositing pyrolytic carbon on porous sheets of carbon material |
| GB1526448A (en) | 1975-01-06 | 1978-09-27 | Pall Corp | Multilayer paper sheet filter cartridges |
| EP0109282A2 (en) | 1982-11-16 | 1984-05-23 | Whatman Reeve Angel Plc | Paper and method of making it |
| US4483771A (en) | 1983-08-08 | 1984-11-20 | Elizabeth Koch | Multi-layer filter |
| DE3341486A1 (en) | 1983-11-17 | 1985-05-30 | Erich W. 5000 Köln Schröder | Air filter |
| US4572428A (en) * | 1985-01-08 | 1986-02-25 | Herrmidifier Company, Inc. | In duct atomizing humidification and evaporative cooling system |
| US4759989A (en) | 1985-11-25 | 1988-07-26 | Kureha Kagaku Kogyo Kabushiki Kaisha | Electrode substrate for fuel cell |
| US4765812A (en) | 1987-10-30 | 1988-08-23 | Allied-Signal Inc. | Air laid filtering material |
| US4851304A (en) | 1987-04-10 | 1989-07-25 | Toray Industries, Inc. | Electrode substrate for fuel cell and process for producing the same |
| US4913856A (en) * | 1988-02-04 | 1990-04-03 | Dri-Steem Humidifier Company | Humidifier system |
| US4925601A (en) | 1988-01-19 | 1990-05-15 | Kimberly-Clark Corporation | Method for making melt-blown liquid filter medium |
| US4980099A (en) * | 1990-01-16 | 1990-12-25 | The Babcock & Wilcox Company | Airfoil lance apparatus for homogeneous humidification and sorbent dispersion in a gas stream |
| US5021284A (en) | 1988-02-24 | 1991-06-04 | Toray Industries, Inc. | Electroconductive integrated substrate and process for producing the same |
| US5108827A (en) | 1989-04-28 | 1992-04-28 | Fiberweb North America, Inc. | Strong nonwoven fabrics from engineered multiconstituent fibers |
| US5167765A (en) | 1990-07-02 | 1992-12-01 | Hoechst Celanese Corporation | Wet laid bonded fibrous web containing bicomponent fibers including lldpe |
| US5178931A (en) | 1990-11-26 | 1993-01-12 | Kimberly-Clark Corporation | Three-layer nonwoven laminiferous structure |
| US5238474A (en) | 1990-10-19 | 1993-08-24 | Donaldson Company, Inc. | Filtration arrangement |
| US5306321A (en) | 1992-07-07 | 1994-04-26 | Donaldson Company, Inc. | Layered air filter medium having improved efficiency and pleatability |
| US5349829A (en) * | 1992-05-21 | 1994-09-27 | Aoc, Inc. | Method and apparatus for evaporatively cooling gases and/or fluids |
| EP0537140B1 (en) | 1990-07-05 | 1994-10-05 | A. Ahlstrom Corporation | Method and apparatus for manufacturing multilayer filter material |
| US5380088A (en) * | 1991-07-30 | 1995-01-10 | Sulzer Brothers Limited | Mixing device for small fluid quantities |
| US5401446A (en) | 1992-10-09 | 1995-03-28 | The University Of Tennessee Research Corporation | Method and apparatus for the electrostatic charging of a web or film |
| US5496507A (en) | 1993-08-17 | 1996-03-05 | Minnesota Mining And Manufacturing Company | Method of charging electret filter media |
| US5516466A (en) * | 1994-10-27 | 1996-05-14 | Armstrong International, Inc. | Steam humidifier system |
| US5571604A (en) | 1993-11-12 | 1996-11-05 | Kimberly-Clark Corporation | Adsorbent fibrous nonwoven composite structure |
| US5580459A (en) | 1992-12-31 | 1996-12-03 | Hoechst Celanese Corporation | Filtration structures of wet laid, bicomponent fiber |
| US5620785A (en) | 1995-06-07 | 1997-04-15 | Fiberweb North America, Inc. | Meltblown barrier webs and processes of making same |
| US5647881A (en) | 1995-04-20 | 1997-07-15 | Minnesota Mining And Manufacturing Company | Shock resistant high efficiency vacuum cleaner filter bag |
| US5648027A (en) | 1993-11-01 | 1997-07-15 | Osaka Gas Company Ltd. | Porous carbonaceous material and a method for producing the same |
| US5653919A (en) * | 1995-06-23 | 1997-08-05 | Morgan & White, Ltd. | Humidification system |
| US5672399A (en) | 1995-11-17 | 1997-09-30 | Donaldson Company, Inc. | Filter material construction and method |
| US5672188A (en) | 1996-05-28 | 1997-09-30 | Aaf International | High capacity filter media |
| EP0847785A1 (en) | 1996-12-12 | 1998-06-17 | Elf Antar France | Device for cleaning slightly contaminated water |
| EP0847786A1 (en) | 1996-12-12 | 1998-06-17 | Elf Antar France | filled paper for gas filtration |
| EP0847784A1 (en) | 1996-12-12 | 1998-06-17 | Elf Antar France | Paper filter for charged liquids |
| US5783503A (en) | 1996-07-22 | 1998-07-21 | Fiberweb North America, Inc. | Meltspun multicomponent thermoplastic continuous filaments, products made therefrom, and methods therefor |
| US5785725A (en) | 1997-04-14 | 1998-07-28 | Johns Manville International, Inc. | Polymeric fiber and glass fiber composite filter media |
| US5908598A (en) | 1995-08-14 | 1999-06-01 | Minnesota Mining And Manufacturing Company | Fibrous webs having enhanced electret properties |
| US5935883A (en) | 1995-11-30 | 1999-08-10 | Kimberly-Clark Worldwide, Inc. | Superfine microfiber nonwoven web |
| US5942163A (en) * | 1997-06-03 | 1999-08-24 | Armstrong International, Inc. | Low pressure jacketed steam manifold |
| US5952251A (en) | 1995-06-30 | 1999-09-14 | Kimberly-Clark Corporation | Coformed dispersible nonwoven fabric bonded with a hybrid system |
| US5955174A (en) | 1995-03-28 | 1999-09-21 | The University Of Tennessee Research Corporation | Composite of pleated and nonwoven webs |
| US5979030A (en) | 1996-04-30 | 1999-11-09 | Minnesota Mining And Manufacturing Company | Synthetic filter media and method for manufacturing same |
| US5993501A (en) | 1996-11-08 | 1999-11-30 | Johns Manville International, Inc. | Composite filter media |
| US6006538A (en) * | 1998-03-09 | 1999-12-28 | Prueitt; Melvin L. | Air conditioner energy system |
| WO2000002006A2 (en) | 1998-07-07 | 2000-01-13 | Siemens Aktiengesellschaft | Method for regulating the magnetization of the bias layer of a magnetoresistive sensor element, sensor element or sensor element system processed according to said method and sensor element and sensor substrate suitable for the implementation of said method |
| US6059866A (en) * | 1997-09-30 | 2000-05-09 | Sanki Engineering Co., Ltd | Air washer |
| DE19854565A1 (en) | 1998-11-26 | 2000-05-31 | Mann & Hummel Filter | Multi-layer filter element |
| US6123752A (en) | 1998-09-03 | 2000-09-26 | 3M Innovative Properties Company | High efficiency synthetic filter medium |
| EP1048335A1 (en) | 1999-04-30 | 2000-11-02 | FiberMark Gessner GmbH & Co. | Dust filter bag containing nonwoven nanofiber fabric |
| US6171684B1 (en) | 1995-11-17 | 2001-01-09 | Donaldson Company, Inc. | Filter material construction and method |
| US6171369B1 (en) | 1998-05-11 | 2001-01-09 | Airflo Europe, N.V. | Vacuum cleaner bag construction and method of operation |
| US6193773B1 (en) | 1998-07-21 | 2001-02-27 | Firma Carl Freudenberg | Dust filter bag |
| US6214094B1 (en) | 1997-10-01 | 2001-04-10 | 3M Innovative Properties Company | Electret filters that exhibit increased oily mist resistance |
| US6213122B1 (en) | 1997-10-01 | 2001-04-10 | 3M Innovative Properties Company | Electret fibers and filter webs having a low level of extractable hydrocarbons |
| US6251224B1 (en) | 1999-08-05 | 2001-06-26 | Owens Corning Fiberglass Technology, Inc. | Bicomponent mats of glass fibers and pulp fibers and their method of manufacture |
| US6261979B1 (en) | 1996-12-04 | 2001-07-17 | Daikin Industries, Ltd. | Filter medium and air filter unit using the same |
| US6267252B1 (en) | 1999-12-08 | 2001-07-31 | Kimberly-Clark Worldwide, Inc. | Fine particle filtration medium including an airlaid composite |
| US20010032714A1 (en) * | 1998-11-09 | 2001-10-25 | Haglid Klas C. | Ventilating system, heat exchanger and methods |
| US20010042361A1 (en) | 2000-02-15 | 2001-11-22 | Cox Stephen T. | Melt blown composite HEPA filter media and vacuum bag |
| WO2001098574A2 (en) | 2000-06-20 | 2001-12-27 | Innovent, Inc. | Multi-drum manufacturing system for nonwoven materials |
| US20020013112A1 (en) | 2000-06-20 | 2002-01-31 | Bontaites George J. | Multi-drum manufacturing system for nonwoven materials |
| WO2002020668A2 (en) | 2000-09-05 | 2002-03-14 | Donaldson Company, Inc. | Polymer compositions, polymer microfibers, polymer nanofibers and applications including filter structure |
| EP0719172B1 (en) | 1993-07-22 | 2002-04-10 | The University Of Tennessee Research Corporation | Post-treatment of laminated nonwoven webs |
| US6372004B1 (en) | 1999-07-08 | 2002-04-16 | Airflo Europe N.V. | High efficiency depth filter and methods of forming the same |
| US6387165B1 (en) * | 2000-02-25 | 2002-05-14 | Oki Electric Industry Co, Ltd. | Airborne molecular contaminant removing apparatus |
| US6398847B1 (en) | 1998-07-02 | 2002-06-04 | 3M Innovative Properties Company | Method of removing contaminants from an aerosol using a new electret article |
| US20020083837A1 (en) | 2000-11-14 | 2002-07-04 | Doherty Joseph P. | Air laid/wet laid gas filtration media |
| US6428610B1 (en) | 2000-01-18 | 2002-08-06 | The University Of Tennessee Research Corporation | Hepa filter |
| US6489051B1 (en) | 1998-05-27 | 2002-12-03 | Toray Industries, Inc. | Carbon fiber paper for solid polymer fuel cells |
| US6488219B1 (en) * | 1999-07-21 | 2002-12-03 | D. Scott Herr | Steam humidifier with pressure variable aperture |
| FR2828114A1 (en) | 2001-07-31 | 2003-02-07 | Ahlstrom Res And Competence Ct | Permeable fibrous material, e.g. useful as a mulching paper, wallhanging paper, dustbag paper, acoustic panel, wiping paper, filter medium or food packaging, includes a germicide adsorbed on activated carbon fibers |
| EP0793990B1 (en) | 1996-03-06 | 2003-03-12 | UFI Universal Filter International S.p.A. | Process for manufacturing a filter medium, the medium manufactured thereby, and filters using said medium |
| US6554881B1 (en) | 1999-10-29 | 2003-04-29 | Hollingsworth & Vose Company | Filter media |
| US20030082979A1 (en) | 2001-10-31 | 2003-05-01 | Kimberly-Clark Worldwide, Inc. | Pulp and conjugate glass fiber composite with enhanced stiffness and permeability |
| WO2003064006A1 (en) | 2002-01-31 | 2003-08-07 | Koslow Technologies Corporation | Nanofiber filter media |
| WO2003064013A1 (en) | 2002-01-31 | 2003-08-07 | Koslow Technologies Corporation | Microporous filter media, filtration systems containing same, and methods of making and using |
| US6623548B1 (en) | 1998-07-18 | 2003-09-23 | Hollingsworth & Vose Air Filtration Limited | Filter materials and methods for the production thereof |
| US6627563B1 (en) | 1999-08-19 | 2003-09-30 | 3M Innovative Properties Company | Oily-mist resistant filter that has nondecreasing efficiency |
| US20030203696A1 (en) | 2002-04-30 | 2003-10-30 | Healey David Thomas | High efficiency ashrae filter media |
| US20030211799A1 (en) | 2001-04-20 | 2003-11-13 | Porex Corporation | Functional fibers and fibrous materials |
| US20030226792A1 (en) | 1998-11-26 | 2003-12-11 | Filterwerk Mann & Hummel Gmbh | Multilayer filter element |
| DE19922326B4 (en) | 1999-05-14 | 2004-02-19 | Mann + Hummel Gmbh | Multi-layer filter medium |
| US20040038014A1 (en) | 2002-08-20 | 2004-02-26 | Donaldson Company, Inc. | Fiber containing filter media |
| US6706086B2 (en) | 2000-10-16 | 2004-03-16 | Fibermark Gressner Gmbh & Co. Kg | Dust filter bag including a highly porous backing material ply |
| US6713034B2 (en) | 2000-01-27 | 2004-03-30 | Mitsubishi Rayon Co., Ltd. | Porous carbon electrode material, method for manufacturing the same, and carbon fiber paper |
| WO2004033069A2 (en) | 2002-10-10 | 2004-04-22 | Ahlstrom Research And Services | Improved filtering medium and use of the said filtering medium for pollution removal from lagoons |
| US20040083695A1 (en) | 2001-03-02 | 2004-05-06 | Jan Schultink | Composite filter and method of making the same |
| US6746517B2 (en) | 2000-09-05 | 2004-06-08 | Donaldson Company, Inc. | Filter structure with two or more layers of fine fiber having extended useful service life |
| US20040112023A1 (en) | 2002-12-12 | 2004-06-17 | Kyung-Ju Choi | Method of forming combined pleated scrim and filter media materials and product of same |
| WO2004069378A2 (en) | 2003-02-05 | 2004-08-19 | Helsa-Werke Helmut Sandler Gmbh & Co. Kg | Filter element and method for the production thereof |
| US20040163540A1 (en) | 2001-06-22 | 2004-08-26 | Hisashi Mori | Filter member |
| US20040211160A1 (en) | 2002-05-16 | 2004-10-28 | Branofilter Gmbh | Multi-layer filter structure and use of a multi-layer filter structure |
| US20040255783A1 (en) | 2003-06-19 | 2004-12-23 | Graham Kristine M. | Cleanable high efficiency filter media structure and applications for use |
| WO2004112956A1 (en) | 2003-06-26 | 2004-12-29 | Ahlstrom Tampere Oy | Method of manufacturing filter material and filter material |
| US20050056313A1 (en) * | 2003-09-12 | 2005-03-17 | Hagen David L. | Method and apparatus for mixing fluids |
| US20050079379A1 (en) | 2003-08-11 | 2005-04-14 | University Of Tennessee Research Foundation | Enhancement of barrier fabrics with breathable films and of face masks and filters with novel fluorochemical electret reinforcing treatment |
| US20050109393A1 (en) | 2003-11-24 | 2005-05-26 | The Boeing Company | Solar electrolysis power source |
| US20050109557A1 (en) | 2003-11-21 | 2005-05-26 | Snecma Moteurs | Soundproofing panel with beads, and a method of manufacture |
| US20050109554A1 (en) | 2003-09-30 | 2005-05-26 | Honda Motor Co., Ltd. | V-belt type continously variable transmission |
| US20050136292A1 (en) | 2003-08-14 | 2005-06-23 | Mariani Robert D. | Thin film dielectrics with perovskite structure and preparation thereof |
| US20050183405A1 (en) | 2000-09-05 | 2005-08-25 | Donaldson Company, Inc. | Air filtration arrangements having fluted media construction and methods |
| US6936554B1 (en) | 2000-11-28 | 2005-08-30 | Kimberly-Clark Worldwide, Inc. | Nonwoven fabric laminate with meltblown web having a gradient fiber size structure |
| US20050193696A1 (en) | 2004-03-02 | 2005-09-08 | Muller Jason W. | Composite filter media |
| US20050212152A1 (en) * | 2004-03-23 | 2005-09-29 | Reens Daniel J | System and method for humidifying homes and commercial sites |
| US20050240517A1 (en) | 2004-04-23 | 2005-10-27 | Rga Reinsurance Company | Automatically administering a non-disinvesting policy loan on an insurance contract |
| US20050241598A1 (en) | 2004-04-28 | 2005-11-03 | Toyota Jidosha Kabushiki Kaisha | Variable valve mechanism |
| US20050250726A1 (en) | 2001-03-29 | 2005-11-10 | University Of Iowa Research Foundation | Immunostimulatory nucleic acid for treatment of non-allergic inflammatory diseases |
| US6977111B2 (en) | 2000-05-22 | 2005-12-20 | Ricoh Company, Ltd. | Multi-layer paper peelable into at least two thin sheets |
| US6986804B2 (en) | 2001-04-07 | 2006-01-17 | 3M Innovative Properties Company | Combination filter for filtering fluids |
| WO2006030407A1 (en) | 2004-09-19 | 2006-03-23 | E.B.T. Interactive Ltd. | Computer-implemented method and system for giving a user an impression of tactile feedback |
| WO2006049664A1 (en) | 2004-11-02 | 2006-05-11 | Kimberly-Clark Worldwide, Inc. | Composite nanofiber materials and methods for making same |
| US20060096260A1 (en) | 2004-11-08 | 2006-05-11 | Bryner Michael A | Filtration media for filtering particulate material from gas streams |
| US20060117728A1 (en) | 2004-12-07 | 2006-06-08 | National Starch And Chemical Investment Holding Corporation | Method of preparing filters |
| US20060137318A1 (en) | 2004-12-28 | 2006-06-29 | Lim Hyun S | Filtration media for filtering particulate material from gas streams |
| WO2006096180A1 (en) | 2005-03-07 | 2006-09-14 | Gore Enterprise Holdings, Inc. | Composite filter media |
| WO2006112563A2 (en) | 2005-04-20 | 2006-10-26 | Nanophil Co., Ltd. | Filter for air cleaning and its manufacturing method |
| EP1721555A1 (en) | 2005-05-12 | 2006-11-15 | MELITTA HAUSHALTSPRODUKTE GmbH & Co. Kommanditgesellschaft | Filter bag |
| US7137510B1 (en) | 1997-11-25 | 2006-11-21 | Filterwerk Mann & Hummel Gmbh | Filter element |
| US20060272303A1 (en) | 2003-03-20 | 2006-12-07 | Ambic Co., Ltd. | Nonwoven fabric air filter for internal combustion engine |
| US20060277877A1 (en) | 2005-06-10 | 2006-12-14 | Lydall, Inc. | High efficiency fuel filter |
| US20060292947A1 (en) | 2005-06-24 | 2006-12-28 | Lavietes Daniel | Polyester fiber scrim and method for making same |
| WO2007024445A1 (en) | 2005-08-19 | 2007-03-01 | Hollingsworth & Vose Company | Hvac meltblown nanoweb filter media |
| US20070054579A1 (en) | 2005-07-29 | 2007-03-08 | Reemay, Inc. | Bicomponent sheet material having liquid barrier properties |
| DE102005055607B3 (en) | 2005-11-22 | 2007-03-22 | Helsa-Automotive Gmbh & Co. Kg | Filter for room ventilation air, particularly for motor vehicles, employs self supporting synthetic fibre fleece with dimpled or corrugated surface finish |
| US20070075015A1 (en) | 2005-09-30 | 2007-04-05 | Bates W D Iii | Filtration media for liquid filtration |
| US20070074628A1 (en) | 2005-09-30 | 2007-04-05 | Jones David C | Coalescing filtration medium and process |
| EP1775006A1 (en) | 2005-10-14 | 2007-04-18 | General Electric Company | Filter, filter media, and methods for making same |
| DE202005019004U1 (en) | 2005-12-06 | 2007-04-19 | Melitta Haushaltsprodukte Gmbh & Co. Kg | Filter material and vacuum cleaner bag |
| US20070125700A1 (en) | 2005-12-05 | 2007-06-07 | Jiang Ding | Nanoweb composite material and gelling method for preparing same |
| WO2007068408A1 (en) | 2005-12-12 | 2007-06-21 | Eurofilters N.V. | Filter bag for a vacuum cleaner and use thereof |
| WO2007068302A1 (en) | 2005-12-13 | 2007-06-21 | Ufi Filters S.P.A. | Method for the realisation of a filtering separator comprising a nanofibre on a substrate with filtering properties |
| WO2007076015A2 (en) | 2005-12-22 | 2007-07-05 | Lydall, Inc. | Composite dual layer hepa filter |
| US7244291B2 (en) | 2005-05-02 | 2007-07-17 | 3M Innovative Properties Company | Electret article having high fluorosaturation ratio |
| US7244292B2 (en) | 2005-05-02 | 2007-07-17 | 3M Innovative Properties Company | Electret article having heteroatoms and low fluorosaturation ratio |
| US20070175195A1 (en) | 2006-01-18 | 2007-08-02 | Skirius Stephen A | Tacky Allergen Trap And Filter Medium, And Method For Containing Allergens |
| US20070175192A1 (en) | 2006-02-01 | 2007-08-02 | Advanced Flow Engineering, Inc. | Pleated hybrid air filter |
| US20070180997A1 (en) | 2006-02-09 | 2007-08-09 | 3M Innovative Properties Company | Electrets and compounds useful in electrets |
| US20070190319A1 (en) | 2006-02-13 | 2007-08-16 | Donaldson Company, Inc. | Polymer blend, polymer solution composition and fibers spun from the polymer blend and filtration applications thereof |
| US20070232175A1 (en) | 2004-09-27 | 2007-10-04 | Takashi Katayama | Binder Fiber and Separator for Alkaline Cell Using Same |
| WO2007112443A2 (en) | 2006-03-28 | 2007-10-04 | North Carolina State University | Micro and nanofiber nonwoven spunbonded fabric |
| US7278542B2 (en) | 2000-08-14 | 2007-10-09 | Ahlstrom Research And Services | Filtering medium, method for making same |
| US20070264520A1 (en) | 2002-12-10 | 2007-11-15 | Wood Willard E | Articles having a polymer grafted cyclodextrin |
| US20070283808A1 (en) | 2001-05-31 | 2007-12-13 | Donaldson Company, Inc. | Air filter with fine fiber and spun bonded media |
| DE102006017553B3 (en) | 2006-04-13 | 2007-12-27 | Eurofilters N.V. | Filter bag for a vacuum cleaner |
| US7314497B2 (en) | 2004-11-05 | 2008-01-01 | Donaldson Company, Inc. | Filter medium and structure |
| DE202007015994U1 (en) | 2007-11-14 | 2008-01-17 | Wolf Pvg Gmbh & Co. Kg | Air filter medium |
| WO2008011450A1 (en) | 2006-07-21 | 2008-01-24 | 3M Innovative Properties Company | High efficiency hvac filter |
| US20080026661A1 (en) | 2006-07-31 | 2008-01-31 | Fox Andrew R | Fibrous web comprising microfibers dispersed among bonded meltspun fibers |
| US20080032110A1 (en) | 2002-12-10 | 2008-02-07 | Cellresin Technologies, Llc | Grafted cyclodextrin |
| US20080060328A1 (en) | 2006-09-12 | 2008-03-13 | Bha Group, Inc. | Filter and filter media |
| US20080069991A1 (en) | 2006-09-13 | 2008-03-20 | Anil Kohli | Bag filter comprising polyphenylene sulfide and acrylic fiber |
| JP2008095266A (en) | 2006-10-12 | 2008-04-24 | Hodai Lee | Conjugate fiber filter using nano material, production equipment of conjugate fiber filter using nano material and production method of conjugate fiber filter using nano material |
| US20080108265A1 (en) | 2006-11-03 | 2008-05-08 | Behnam Pourdeyhimi | High surface area fiber and textiles made from the same |
| US20080105626A1 (en) | 2006-11-02 | 2008-05-08 | David Charles Jones | Fuel filter |
| WO2008052970A1 (en) | 2006-10-31 | 2008-05-08 | Basf Se | Method for producing a multi layer fiber web from cellulose fibers |
| WO2008066813A2 (en) | 2006-11-27 | 2008-06-05 | E. I. Du Pont De Nemours And Company | Durable nanoweb scrim laminates |
| WO2008103821A2 (en) | 2007-02-23 | 2008-08-28 | Donaldson Company, Inc. | Formed filter element |
| US20080202078A1 (en) | 2007-02-28 | 2008-08-28 | Hollingsworth & Vose Company | Waved filter media and elements |
| US20080245037A1 (en) | 2005-02-04 | 2008-10-09 | Robert Rogers | Aerosol Separator; and Method |
| US20080302242A1 (en) | 2007-06-07 | 2008-12-11 | Antoine Schelling | Process for forming a laminate of a nanoweb and a substrate and filters using the laminate |
| US20090044702A1 (en) | 2007-02-22 | 2009-02-19 | Adamek Daniel E | Filter element and method |
| US20090120868A1 (en) | 2007-09-19 | 2009-05-14 | Mann+Hummel Gmbh | Transmission Oil Filter Comprising a Melt Blown Layer at the Downstream Side |
| US20090120048A1 (en) | 2007-11-09 | 2009-05-14 | Hollingsworth & Vose Company | Meltblown Filter Medium |
| US20100000411A1 (en) | 2007-11-09 | 2010-01-07 | Hollingsworth & Vose Company | Meltblown filter medium, related applications and uses |
| US20100116138A1 (en) | 2008-11-07 | 2010-05-13 | Hollingsworth & Vose Company | Multi-phase filter medium |
| US20100187171A1 (en) | 2009-01-28 | 2010-07-29 | Donaldson Company, Inc. | Fibrous Media |
| US7887889B2 (en) | 2001-12-14 | 2011-02-15 | 3M Innovative Properties Company | Plasma fluorination treatment of porous materials |
| US20110147320A1 (en) * | 2009-12-22 | 2011-06-23 | Hollingsworth & Vose Company | Filter media and articles including dendrimers and/or other components |
| US20120152824A1 (en) | 2010-12-17 | 2012-06-21 | Hollingsworth & Vose Company | Fine fiber filter media and processes |
| US20120152821A1 (en) | 2010-12-17 | 2012-06-21 | Hollingsworth & Vose Company | Fine fiber filter media and processes |
| US20120318754A1 (en) | 2010-12-17 | 2012-12-20 | Hollingsworth & Vose Company | Fine fiber filter media and processes |
| US8679218B2 (en) * | 2010-04-27 | 2014-03-25 | Hollingsworth & Vose Company | Filter media with a multi-layer structure |
| US8679217B2 (en) | 2007-09-07 | 2014-03-25 | E I Du Pont De Nemours And Company | Pleated nanoweb structures |
| US20140130469A1 (en) | 2012-11-13 | 2014-05-15 | Hollingsworth & Vose Company | Multi-layered filter media |
| US20140214340A1 (en) * | 2011-07-15 | 2014-07-31 | Voestalpine Stahl Gmbh | Apparatus and method for detecting at least one periodically occurring defect on an object |
| US20140346107A1 (en) | 2013-05-24 | 2014-11-27 | Hollingsworth & Vose Company | Filter Media Including Polymer Compositions and Blends |
| US8950587B2 (en) | 2009-04-03 | 2015-02-10 | Hollingsworth & Vose Company | Filter media suitable for hydraulic applications |
| US8973906B2 (en) * | 2010-02-05 | 2015-03-10 | Klingenburg Gmbh | Device for conditioning an air flow |
| US20150121823A1 (en) * | 2007-02-28 | 2015-05-07 | Hollingsworth & Vose Company | Waved filter media and elements |
| US20150167249A1 (en) | 2012-07-19 | 2015-06-18 | Aahi Kasei Fibers Corporation | Multilayered structure comprising fine fiber cellulose layer |
| US20160059167A1 (en) | 2012-11-13 | 2016-03-03 | Hollingsworth & Vose Company | Pre-coalescing multi-layered filter media |
| US9289632B2 (en) | 2010-05-07 | 2016-03-22 | Japan Vilene Company, Ltd. | Electrically charged filter and mask |
| US20160166953A1 (en) | 2014-12-15 | 2016-06-16 | Hollingsworth & Vose Company | Filter media including fine staple fibers |
| US20160175752A1 (en) | 2014-12-19 | 2016-06-23 | Hollingsworth & Vose Company | Filter media comprising a pre-filter layer |
| US20160361674A1 (en) | 2014-12-15 | 2016-12-15 | Hollingsworth & Vose Company | Filter media including fine staple fibers |
| US20170248334A1 (en) * | 2014-10-29 | 2017-08-31 | Merlin Technology Gmbh | Apparatus for humidifying air in an air duct |
| US20180001244A1 (en) | 2016-07-01 | 2018-01-04 | Hollingsworth & Vose Company | Multi-layered electret-containing filtration media |
| US20180023824A1 (en) * | 2015-02-13 | 2018-01-25 | Merlin Technology Gmbh | Long-range nozzle for entry of air |
| US20180236384A1 (en) | 2017-02-21 | 2018-08-23 | Hollingsworth & Vose Company | Electret-containing filter media |
| US20180236389A1 (en) | 2017-02-21 | 2018-08-23 | Hollingsworth & Vose Company | Electret-containing filter media |
| US20180236385A1 (en) | 2017-02-21 | 2018-08-23 | Hollingsworth & Vose Company | Electret-containing filter media |
| US20180243674A1 (en) | 2017-02-21 | 2018-08-30 | Hollingsworth & Vose Company | Electret-containing filter media |
| US20220381455A1 (en) * | 2021-06-01 | 2022-12-01 | Shenzhen Envicool Technology Co., Ltd. | Indirect evaporative cooling air conditioner |
-
2016
- 2016-07-22 US US15/217,718 patent/US12420221B2/en active Active
Patent Citations (290)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US853981A (en) | 1906-05-29 | 1907-05-21 | George Kneuper | Filtering material. |
| US2208443A (en) * | 1938-04-06 | 1940-07-16 | Carrier Corp | Air conditioning method and apparatus |
| US2235005A (en) * | 1938-04-06 | 1941-03-18 | Carrier Corp | Air conditioning method |
| US2196821A (en) | 1938-05-14 | 1940-04-09 | Motor Improvements Inc | Filter |
| US2392901A (en) | 1943-03-20 | 1946-01-15 | Cleo E Brown | Filter |
| US2663156A (en) * | 1952-03-24 | 1953-12-22 | Jess F Baker | Apparatus for cooling and dehumidifying air |
| US2928765A (en) | 1957-02-11 | 1960-03-15 | C H Dexter & Sons Inc | Air filter paper and method of making same |
| US3353800A (en) * | 1965-01-11 | 1967-11-21 | Detrick M H Co | Apparatus for removing solids from hot gases |
| US3656882A (en) | 1970-03-09 | 1972-04-18 | Celanese Corp | ACRYLIC FIBER STABILIZATION CATALYZED BY Co(II) AND Ce(III) CATIONS |
| US3654851A (en) * | 1970-04-08 | 1972-04-11 | Mannie Bertin | Diffusers for conditioned air conduits |
| US3855133A (en) | 1971-12-28 | 1974-12-17 | Sartorius Membranfilter Gmbh | Multi-layer filter membrane |
| US3908528A (en) * | 1973-07-30 | 1975-09-30 | Mannie Bertin | Diffusers for conditioned air |
| US3944686A (en) | 1974-06-19 | 1976-03-16 | Pfizer Inc. | Method for vapor depositing pyrolytic carbon on porous sheets of carbon material |
| US4048953A (en) | 1974-06-19 | 1977-09-20 | Pfizer Inc. | Apparatus for vapor depositing pyrolytic carbon on porous sheets of carbon material |
| US4033881A (en) | 1975-01-06 | 1977-07-05 | Pall Corporation | Multilayer paper sheet filter cartridges |
| GB1526448A (en) | 1975-01-06 | 1978-09-27 | Pall Corp | Multilayer paper sheet filter cartridges |
| EP0109282A2 (en) | 1982-11-16 | 1984-05-23 | Whatman Reeve Angel Plc | Paper and method of making it |
| US4483771A (en) | 1983-08-08 | 1984-11-20 | Elizabeth Koch | Multi-layer filter |
| DE3341486A1 (en) | 1983-11-17 | 1985-05-30 | Erich W. 5000 Köln Schröder | Air filter |
| US4572428A (en) * | 1985-01-08 | 1986-02-25 | Herrmidifier Company, Inc. | In duct atomizing humidification and evaporative cooling system |
| US4759989A (en) | 1985-11-25 | 1988-07-26 | Kureha Kagaku Kogyo Kabushiki Kaisha | Electrode substrate for fuel cell |
| US4851304A (en) | 1987-04-10 | 1989-07-25 | Toray Industries, Inc. | Electrode substrate for fuel cell and process for producing the same |
| US4765812A (en) | 1987-10-30 | 1988-08-23 | Allied-Signal Inc. | Air laid filtering material |
| US4925601A (en) | 1988-01-19 | 1990-05-15 | Kimberly-Clark Corporation | Method for making melt-blown liquid filter medium |
| US4913856A (en) * | 1988-02-04 | 1990-04-03 | Dri-Steem Humidifier Company | Humidifier system |
| US5021284A (en) | 1988-02-24 | 1991-06-04 | Toray Industries, Inc. | Electroconductive integrated substrate and process for producing the same |
| US5108827A (en) | 1989-04-28 | 1992-04-28 | Fiberweb North America, Inc. | Strong nonwoven fabrics from engineered multiconstituent fibers |
| US4980099A (en) * | 1990-01-16 | 1990-12-25 | The Babcock & Wilcox Company | Airfoil lance apparatus for homogeneous humidification and sorbent dispersion in a gas stream |
| US5167765A (en) | 1990-07-02 | 1992-12-01 | Hoechst Celanese Corporation | Wet laid bonded fibrous web containing bicomponent fibers including lldpe |
| EP0537140B1 (en) | 1990-07-05 | 1994-10-05 | A. Ahlstrom Corporation | Method and apparatus for manufacturing multilayer filter material |
| US5238474A (en) | 1990-10-19 | 1993-08-24 | Donaldson Company, Inc. | Filtration arrangement |
| US5178931A (en) | 1990-11-26 | 1993-01-12 | Kimberly-Clark Corporation | Three-layer nonwoven laminiferous structure |
| US5380088A (en) * | 1991-07-30 | 1995-01-10 | Sulzer Brothers Limited | Mixing device for small fluid quantities |
| US5349829A (en) * | 1992-05-21 | 1994-09-27 | Aoc, Inc. | Method and apparatus for evaporatively cooling gases and/or fluids |
| US5306321A (en) | 1992-07-07 | 1994-04-26 | Donaldson Company, Inc. | Layered air filter medium having improved efficiency and pleatability |
| US5401446A (en) | 1992-10-09 | 1995-03-28 | The University Of Tennessee Research Corporation | Method and apparatus for the electrostatic charging of a web or film |
| US5580459A (en) | 1992-12-31 | 1996-12-03 | Hoechst Celanese Corporation | Filtration structures of wet laid, bicomponent fiber |
| EP0719172B1 (en) | 1993-07-22 | 2002-04-10 | The University Of Tennessee Research Corporation | Post-treatment of laminated nonwoven webs |
| US5496507A (en) | 1993-08-17 | 1996-03-05 | Minnesota Mining And Manufacturing Company | Method of charging electret filter media |
| US5648027A (en) | 1993-11-01 | 1997-07-15 | Osaka Gas Company Ltd. | Porous carbonaceous material and a method for producing the same |
| US5571604A (en) | 1993-11-12 | 1996-11-05 | Kimberly-Clark Corporation | Adsorbent fibrous nonwoven composite structure |
| US5516466A (en) * | 1994-10-27 | 1996-05-14 | Armstrong International, Inc. | Steam humidifier system |
| US5955174A (en) | 1995-03-28 | 1999-09-21 | The University Of Tennessee Research Corporation | Composite of pleated and nonwoven webs |
| US5647881A (en) | 1995-04-20 | 1997-07-15 | Minnesota Mining And Manufacturing Company | Shock resistant high efficiency vacuum cleaner filter bag |
| US5620785A (en) | 1995-06-07 | 1997-04-15 | Fiberweb North America, Inc. | Meltblown barrier webs and processes of making same |
| US5653919A (en) * | 1995-06-23 | 1997-08-05 | Morgan & White, Ltd. | Humidification system |
| US5952251A (en) | 1995-06-30 | 1999-09-14 | Kimberly-Clark Corporation | Coformed dispersible nonwoven fabric bonded with a hybrid system |
| US6268495B1 (en) | 1995-08-14 | 2001-07-31 | 3M Innovative Properties Company | Compounds useful as resin additives |
| US6002017A (en) | 1995-08-14 | 1999-12-14 | Minnesota Mining And Manufacturing Company | Compounds useful as resin additives |
| US5976208A (en) | 1995-08-14 | 1999-11-02 | Minnesota Mining And Manufacturing Company | Electret filter media containing filtration enhancing additives |
| US5968635A (en) | 1995-08-14 | 1999-10-19 | Minnesota Mining And Manufacturing Company | Fibrous webs useful for making electret filter media |
| US5919847A (en) | 1995-08-14 | 1999-07-06 | Minnesota Mining And Manufacturing Company | Composition useful for making electret fibers |
| US5908598A (en) | 1995-08-14 | 1999-06-01 | Minnesota Mining And Manufacturing Company | Fibrous webs having enhanced electret properties |
| US5672399A (en) | 1995-11-17 | 1997-09-30 | Donaldson Company, Inc. | Filter material construction and method |
| US6171684B1 (en) | 1995-11-17 | 2001-01-09 | Donaldson Company, Inc. | Filter material construction and method |
| US20050210844A1 (en) | 1995-11-17 | 2005-09-29 | Donaldson Company, Inc. | Filter material construction and method |
| US5935883A (en) | 1995-11-30 | 1999-08-10 | Kimberly-Clark Worldwide, Inc. | Superfine microfiber nonwoven web |
| EP0793990B1 (en) | 1996-03-06 | 2003-03-12 | UFI Universal Filter International S.p.A. | Process for manufacturing a filter medium, the medium manufactured thereby, and filters using said medium |
| US6211100B1 (en) | 1996-04-30 | 2001-04-03 | Minnesota Mining And Manufacturing Company | Synthetic filter media |
| US5979030A (en) | 1996-04-30 | 1999-11-09 | Minnesota Mining And Manufacturing Company | Synthetic filter media and method for manufacturing same |
| US5672188A (en) | 1996-05-28 | 1997-09-30 | Aaf International | High capacity filter media |
| US5783503A (en) | 1996-07-22 | 1998-07-21 | Fiberweb North America, Inc. | Meltspun multicomponent thermoplastic continuous filaments, products made therefrom, and methods therefor |
| US5993501A (en) | 1996-11-08 | 1999-11-30 | Johns Manville International, Inc. | Composite filter media |
| US6261979B1 (en) | 1996-12-04 | 2001-07-17 | Daikin Industries, Ltd. | Filter medium and air filter unit using the same |
| EP0847786A1 (en) | 1996-12-12 | 1998-06-17 | Elf Antar France | filled paper for gas filtration |
| JPH10230114A (en) | 1996-12-12 | 1998-09-02 | Elf Antar Fr | Paper containing filler for filtering gas |
| EP0847785A1 (en) | 1996-12-12 | 1998-06-17 | Elf Antar France | Device for cleaning slightly contaminated water |
| EP0847784A1 (en) | 1996-12-12 | 1998-06-17 | Elf Antar France | Paper filter for charged liquids |
| US5785725A (en) | 1997-04-14 | 1998-07-28 | Johns Manville International, Inc. | Polymeric fiber and glass fiber composite filter media |
| US5942163A (en) * | 1997-06-03 | 1999-08-24 | Armstrong International, Inc. | Low pressure jacketed steam manifold |
| US6059866A (en) * | 1997-09-30 | 2000-05-09 | Sanki Engineering Co., Ltd | Air washer |
| US6238466B1 (en) | 1997-10-01 | 2001-05-29 | 3M Innovative Properties Company | Electret articles and filters with increased oily mist resistance |
| US6261342B1 (en) | 1997-10-01 | 2001-07-17 | 3M Innovative Properties Company | Method of removing particulate solid or liquid aerosol from a gas |
| US6214094B1 (en) | 1997-10-01 | 2001-04-10 | 3M Innovative Properties Company | Electret filters that exhibit increased oily mist resistance |
| US6213122B1 (en) | 1997-10-01 | 2001-04-10 | 3M Innovative Properties Company | Electret fibers and filter webs having a low level of extractable hydrocarbons |
| US7137510B1 (en) | 1997-11-25 | 2006-11-21 | Filterwerk Mann & Hummel Gmbh | Filter element |
| US6006538A (en) * | 1998-03-09 | 1999-12-28 | Prueitt; Melvin L. | Air conditioner energy system |
| US6183536B1 (en) | 1998-05-11 | 2001-02-06 | Airflo Europe, N.V. | Enhanced performance vacuum cleaner bag and method of operation |
| US6171369B1 (en) | 1998-05-11 | 2001-01-09 | Airflo Europe, N.V. | Vacuum cleaner bag construction and method of operation |
| US6489051B1 (en) | 1998-05-27 | 2002-12-03 | Toray Industries, Inc. | Carbon fiber paper for solid polymer fuel cells |
| US6660210B2 (en) | 1998-07-02 | 2003-12-09 | 3M Innovative Properties Company | Method of making fluorinated electrets |
| US6808551B2 (en) | 1998-07-02 | 2004-10-26 | 3M Innovative Properties Company | Method of using fluorinated electrets |
| US6562112B2 (en) | 1998-07-02 | 2003-05-13 | 3M Innovative Properties Company | Fluorinated electret |
| US6953544B2 (en) | 1998-07-02 | 2005-10-11 | 3M Innovative Properties Company | Method of making a respirator that has a fluorinated electret |
| US6397458B1 (en) | 1998-07-02 | 2002-06-04 | 3M Innovative Properties Company | Method of making an electret article by transferring fluorine to the article from a gaseous phase |
| US6432175B1 (en) | 1998-07-02 | 2002-08-13 | 3M Innovative Properties Company | Fluorinated electret |
| US6409806B1 (en) | 1998-07-02 | 2002-06-25 | 3M Innovative Properties Company | Fluorinated electret |
| US6398847B1 (en) | 1998-07-02 | 2002-06-04 | 3M Innovative Properties Company | Method of removing contaminants from an aerosol using a new electret article |
| WO2000002006A2 (en) | 1998-07-07 | 2000-01-13 | Siemens Aktiengesellschaft | Method for regulating the magnetization of the bias layer of a magnetoresistive sensor element, sensor element or sensor element system processed according to said method and sensor element and sensor substrate suitable for the implementation of said method |
| US6623548B1 (en) | 1998-07-18 | 2003-09-23 | Hollingsworth & Vose Air Filtration Limited | Filter materials and methods for the production thereof |
| US6193773B1 (en) | 1998-07-21 | 2001-02-27 | Firma Carl Freudenberg | Dust filter bag |
| US6123752A (en) | 1998-09-03 | 2000-09-26 | 3M Innovative Properties Company | High efficiency synthetic filter medium |
| US20010032714A1 (en) * | 1998-11-09 | 2001-10-25 | Haglid Klas C. | Ventilating system, heat exchanger and methods |
| US20030226792A1 (en) | 1998-11-26 | 2003-12-11 | Filterwerk Mann & Hummel Gmbh | Multilayer filter element |
| DE19854565A1 (en) | 1998-11-26 | 2000-05-31 | Mann & Hummel Filter | Multi-layer filter element |
| EP1048335B1 (en) | 1999-04-30 | 2005-04-13 | FiberMark Gessner GmbH & Co. | Dust filter bag containing nonwoven nanofiber fabric |
| EP1048335A1 (en) | 1999-04-30 | 2000-11-02 | FiberMark Gessner GmbH & Co. | Dust filter bag containing nonwoven nanofiber fabric |
| DE19922326B4 (en) | 1999-05-14 | 2004-02-19 | Mann + Hummel Gmbh | Multi-layer filter medium |
| US6372004B1 (en) | 1999-07-08 | 2002-04-16 | Airflo Europe N.V. | High efficiency depth filter and methods of forming the same |
| US6488219B1 (en) * | 1999-07-21 | 2002-12-03 | D. Scott Herr | Steam humidifier with pressure variable aperture |
| US6251224B1 (en) | 1999-08-05 | 2001-06-26 | Owens Corning Fiberglass Technology, Inc. | Bicomponent mats of glass fibers and pulp fibers and their method of manufacture |
| US6627563B1 (en) | 1999-08-19 | 2003-09-30 | 3M Innovative Properties Company | Oily-mist resistant filter that has nondecreasing efficiency |
| US6858057B2 (en) | 1999-10-29 | 2005-02-22 | Hollingsworth & Vosa Company | Filter media |
| US6554881B1 (en) | 1999-10-29 | 2003-04-29 | Hollingsworth & Vose Company | Filter media |
| US6267252B1 (en) | 1999-12-08 | 2001-07-31 | Kimberly-Clark Worldwide, Inc. | Fine particle filtration medium including an airlaid composite |
| US6428610B1 (en) | 2000-01-18 | 2002-08-06 | The University Of Tennessee Research Corporation | Hepa filter |
| US6713034B2 (en) | 2000-01-27 | 2004-03-30 | Mitsubishi Rayon Co., Ltd. | Porous carbon electrode material, method for manufacturing the same, and carbon fiber paper |
| US20010042361A1 (en) | 2000-02-15 | 2001-11-22 | Cox Stephen T. | Melt blown composite HEPA filter media and vacuum bag |
| US6387165B1 (en) * | 2000-02-25 | 2002-05-14 | Oki Electric Industry Co, Ltd. | Airborne molecular contaminant removing apparatus |
| US6977111B2 (en) | 2000-05-22 | 2005-12-20 | Ricoh Company, Ltd. | Multi-layer paper peelable into at least two thin sheets |
| WO2001098574A2 (en) | 2000-06-20 | 2001-12-27 | Innovent, Inc. | Multi-drum manufacturing system for nonwoven materials |
| US20020013112A1 (en) | 2000-06-20 | 2002-01-31 | Bontaites George J. | Multi-drum manufacturing system for nonwoven materials |
| US7278542B2 (en) | 2000-08-14 | 2007-10-09 | Ahlstrom Research And Services | Filtering medium, method for making same |
| US7318852B2 (en) | 2000-09-05 | 2008-01-15 | Donaldson Company, Inc. | Bag house filter with fine fiber and spun bonded media |
| US6924028B2 (en) | 2000-09-05 | 2005-08-02 | Donaldson Company, Inc. | Polymer, polymer microfiber, polymer nanofiber and applications including filter structures |
| WO2002020668A2 (en) | 2000-09-05 | 2002-03-14 | Donaldson Company, Inc. | Polymer compositions, polymer microfibers, polymer nanofibers and applications including filter structure |
| US6955775B2 (en) | 2000-09-05 | 2005-10-18 | Donaldson Company, Inc. | Process if making fine fiber material |
| US20040123572A1 (en) | 2000-09-05 | 2004-07-01 | Donaldson Company, Inc. | Polymer, polymer microfiber, polymer nanofiber and applications including filter structures |
| US20080110822A1 (en) | 2000-09-05 | 2008-05-15 | Donaldson Company, Inc. | Fine fiber media layer |
| US20030106294A1 (en) | 2000-09-05 | 2003-06-12 | Chung Hoo Y. | Polymer, polymer microfiber, polymer nanofiber and applications including filter structures |
| US20040187454A1 (en) | 2000-09-05 | 2004-09-30 | Donaldson Company, Inc. | Polymer, polymer microfiber, polymer nanofiber and applications including filter structures |
| US6746517B2 (en) | 2000-09-05 | 2004-06-08 | Donaldson Company, Inc. | Filter structure with two or more layers of fine fiber having extended useful service life |
| US7179317B2 (en) | 2000-09-05 | 2007-02-20 | Donaldson Company, Inc. | Polymer, polymer microfiber, polymer nanofiber and applications including filter structures |
| US6743273B2 (en) | 2000-09-05 | 2004-06-01 | Donaldson Company, Inc. | Polymer, polymer microfiber, polymer nanofiber and applications including filter structures |
| US20070271883A1 (en) | 2000-09-05 | 2007-11-29 | Donaldson Company, Inc. | Bag house filter with fine fiber and spun bonded media |
| US7070640B2 (en) | 2000-09-05 | 2006-07-04 | Donaldson Company, Inc. | Polymer, polymer microfiber, polymer nanofiber and applications including filter structures |
| US20040060269A1 (en) | 2000-09-05 | 2004-04-01 | Donaldson Company, Inc. | Polymer, polymer microfiber, polymer nanofiber and applications including filter structures |
| US20040060268A1 (en) | 2000-09-05 | 2004-04-01 | Donaldson Company, Inc. | Polymer, polymer microfiber, polymer nanofiber and applications including filter structures |
| US20050183405A1 (en) | 2000-09-05 | 2005-08-25 | Donaldson Company, Inc. | Air filtration arrangements having fluted media construction and methods |
| US6706086B2 (en) | 2000-10-16 | 2004-03-16 | Fibermark Gressner Gmbh & Co. Kg | Dust filter bag including a highly porous backing material ply |
| US6579350B2 (en) | 2000-11-14 | 2003-06-17 | Lydall, Inc. | Air laid/wet laid gas filtration media |
| US20020083837A1 (en) | 2000-11-14 | 2002-07-04 | Doherty Joseph P. | Air laid/wet laid gas filtration media |
| US6936554B1 (en) | 2000-11-28 | 2005-08-30 | Kimberly-Clark Worldwide, Inc. | Nonwoven fabric laminate with meltblown web having a gradient fiber size structure |
| US20040083695A1 (en) | 2001-03-02 | 2004-05-06 | Jan Schultink | Composite filter and method of making the same |
| US20050250726A1 (en) | 2001-03-29 | 2005-11-10 | University Of Iowa Research Foundation | Immunostimulatory nucleic acid for treatment of non-allergic inflammatory diseases |
| US6986804B2 (en) | 2001-04-07 | 2006-01-17 | 3M Innovative Properties Company | Combination filter for filtering fluids |
| US20030211799A1 (en) | 2001-04-20 | 2003-11-13 | Porex Corporation | Functional fibers and fibrous materials |
| US20070283808A1 (en) | 2001-05-31 | 2007-12-13 | Donaldson Company, Inc. | Air filter with fine fiber and spun bonded media |
| US7316723B2 (en) | 2001-05-31 | 2008-01-08 | Donaldson Company, Inc. | Air filter with fine fiber and spun bonded media |
| US20040163540A1 (en) | 2001-06-22 | 2004-08-26 | Hisashi Mori | Filter member |
| FR2828114A1 (en) | 2001-07-31 | 2003-02-07 | Ahlstrom Res And Competence Ct | Permeable fibrous material, e.g. useful as a mulching paper, wallhanging paper, dustbag paper, acoustic panel, wiping paper, filter medium or food packaging, includes a germicide adsorbed on activated carbon fibers |
| US20030082979A1 (en) | 2001-10-31 | 2003-05-01 | Kimberly-Clark Worldwide, Inc. | Pulp and conjugate glass fiber composite with enhanced stiffness and permeability |
| US9127363B2 (en) | 2001-12-14 | 2015-09-08 | 3M Innovative Properties Company | Fluorinated porous article |
| US7887889B2 (en) | 2001-12-14 | 2011-02-15 | 3M Innovative Properties Company | Plasma fluorination treatment of porous materials |
| US6872311B2 (en) | 2002-01-31 | 2005-03-29 | Koslow Technologies Corporation | Nanofiber filter media |
| US20030213750A1 (en) | 2002-01-31 | 2003-11-20 | Koslow Evan E. | Microporous filter media, filtration systems containing same, and methods of making and using |
| US20030196964A1 (en) | 2002-01-31 | 2003-10-23 | Koslow Evan E. | Microporous filter media, filteration systems containing same, and methods of making and using |
| US20030168401A1 (en) | 2002-01-31 | 2003-09-11 | Koslow Evan E. | Microporous filter media, filtration systems containing same, and methods of making and using |
| WO2003064013A1 (en) | 2002-01-31 | 2003-08-07 | Koslow Technologies Corporation | Microporous filter media, filtration systems containing same, and methods of making and using |
| US20030201231A1 (en) | 2002-01-31 | 2003-10-30 | Koslow Evan E. | Microporous filter media, filtration systems containing same, and methods of making and using |
| US20030177909A1 (en) | 2002-01-31 | 2003-09-25 | Koslow Evan E. | Nanofiber filter media |
| EP1483039B1 (en) | 2002-01-31 | 2008-04-23 | KX Technologies LLC | Microporous filter media, filtration systems containing same, and methods of making and using |
| US20030205530A1 (en) | 2002-01-31 | 2003-11-06 | Koslow Evan E. | Microporous filter media, filtration systems containing same, and methods of making and using |
| US20030196963A1 (en) | 2002-01-31 | 2003-10-23 | Koslow Evan E. | Microporous filter media, filtration systems containing same, and methods of making and using |
| US20030205529A1 (en) | 2002-01-31 | 2003-11-06 | Koslow Evan E. | Microporous filter media, filtration systems containing same, and methods of making and using |
| US20030205531A1 (en) | 2002-01-31 | 2003-11-06 | Koslow Evan E. | Microporous filter media, filtration systems containing same, and methods of making and using |
| US7144533B2 (en) | 2002-01-31 | 2006-12-05 | Koslow Technologies Corporation | Microporous filter media, filtration systems containing same, and methods of making and using |
| WO2003064006A1 (en) | 2002-01-31 | 2003-08-07 | Koslow Technologies Corporation | Nanofiber filter media |
| US20030203696A1 (en) | 2002-04-30 | 2003-10-30 | Healey David Thomas | High efficiency ashrae filter media |
| US20040211160A1 (en) | 2002-05-16 | 2004-10-28 | Branofilter Gmbh | Multi-layer filter structure and use of a multi-layer filter structure |
| US20040038014A1 (en) | 2002-08-20 | 2004-02-26 | Donaldson Company, Inc. | Fiber containing filter media |
| WO2004028662A2 (en) | 2002-09-26 | 2004-04-08 | Hollingsworth & Vose Company | High efficiency ashrae filter media |
| WO2004033069A2 (en) | 2002-10-10 | 2004-04-22 | Ahlstrom Research And Services | Improved filtering medium and use of the said filtering medium for pollution removal from lagoons |
| US7578938B2 (en) | 2002-10-10 | 2009-08-25 | Ahlstrom Corporation | Filtering medium and use of the said filtering medium for pollution removal from lagoons |
| US20070264520A1 (en) | 2002-12-10 | 2007-11-15 | Wood Willard E | Articles having a polymer grafted cyclodextrin |
| US20080032110A1 (en) | 2002-12-10 | 2008-02-07 | Cellresin Technologies, Llc | Grafted cyclodextrin |
| US20040112023A1 (en) | 2002-12-12 | 2004-06-17 | Kyung-Ju Choi | Method of forming combined pleated scrim and filter media materials and product of same |
| WO2004069378A2 (en) | 2003-02-05 | 2004-08-19 | Helsa-Werke Helmut Sandler Gmbh & Co. Kg | Filter element and method for the production thereof |
| US20060272303A1 (en) | 2003-03-20 | 2006-12-07 | Ambic Co., Ltd. | Nonwoven fabric air filter for internal combustion engine |
| US7008465B2 (en) | 2003-06-19 | 2006-03-07 | Donaldson Company, Inc. | Cleanable high efficiency filter media structure and applications for use |
| US20040255783A1 (en) | 2003-06-19 | 2004-12-23 | Graham Kristine M. | Cleanable high efficiency filter media structure and applications for use |
| WO2004112937A1 (en) | 2003-06-19 | 2004-12-29 | Donaldson Company, Inc. | Cleanable high efficiency filter media structure and applications for use |
| WO2004112956A1 (en) | 2003-06-26 | 2004-12-29 | Ahlstrom Tampere Oy | Method of manufacturing filter material and filter material |
| US20050079379A1 (en) | 2003-08-11 | 2005-04-14 | University Of Tennessee Research Foundation | Enhancement of barrier fabrics with breathable films and of face masks and filters with novel fluorochemical electret reinforcing treatment |
| WO2005034659A2 (en) | 2003-08-11 | 2005-04-21 | University Of Tennessee Research Foundation | Fluorochemical electret treatment for barrier fabrics |
| US20050136292A1 (en) | 2003-08-14 | 2005-06-23 | Mariani Robert D. | Thin film dielectrics with perovskite structure and preparation thereof |
| US20050056313A1 (en) * | 2003-09-12 | 2005-03-17 | Hagen David L. | Method and apparatus for mixing fluids |
| US20050109554A1 (en) | 2003-09-30 | 2005-05-26 | Honda Motor Co., Ltd. | V-belt type continously variable transmission |
| US20050109557A1 (en) | 2003-11-21 | 2005-05-26 | Snecma Moteurs | Soundproofing panel with beads, and a method of manufacture |
| US20050109393A1 (en) | 2003-11-24 | 2005-05-26 | The Boeing Company | Solar electrolysis power source |
| US20050193696A1 (en) | 2004-03-02 | 2005-09-08 | Muller Jason W. | Composite filter media |
| US8128069B2 (en) * | 2004-03-23 | 2012-03-06 | Reens Daniel J | System and method for humidifying homes and commercial sites |
| US20050212152A1 (en) * | 2004-03-23 | 2005-09-29 | Reens Daniel J | System and method for humidifying homes and commercial sites |
| US20050240517A1 (en) | 2004-04-23 | 2005-10-27 | Rga Reinsurance Company | Automatically administering a non-disinvesting policy loan on an insurance contract |
| US20050241598A1 (en) | 2004-04-28 | 2005-11-03 | Toyota Jidosha Kabushiki Kaisha | Variable valve mechanism |
| WO2006030407A1 (en) | 2004-09-19 | 2006-03-23 | E.B.T. Interactive Ltd. | Computer-implemented method and system for giving a user an impression of tactile feedback |
| US20070232175A1 (en) | 2004-09-27 | 2007-10-04 | Takashi Katayama | Binder Fiber and Separator for Alkaline Cell Using Same |
| WO2006049664A1 (en) | 2004-11-02 | 2006-05-11 | Kimberly-Clark Worldwide, Inc. | Composite nanofiber materials and methods for making same |
| US20080160856A1 (en) | 2004-11-02 | 2008-07-03 | Kimberly-Clark Worldwide, Inc. | Composite nanofiber materials and methods for making same |
| US7390760B1 (en) | 2004-11-02 | 2008-06-24 | Kimberly-Clark Worldwide, Inc. | Composite nanofiber materials and methods for making same |
| US7314497B2 (en) | 2004-11-05 | 2008-01-01 | Donaldson Company, Inc. | Filter medium and structure |
| US7235122B2 (en) | 2004-11-08 | 2007-06-26 | E. I. Du Pont De Nemours And Company | Filtration media for filtering particulate material from gas streams |
| US20060096260A1 (en) | 2004-11-08 | 2006-05-11 | Bryner Michael A | Filtration media for filtering particulate material from gas streams |
| WO2006053295A1 (en) | 2004-11-08 | 2006-05-18 | E.I. Dupont De Nemours And Company | Filtration media for filtering particulate material from gas streams |
| US20060117728A1 (en) | 2004-12-07 | 2006-06-08 | National Starch And Chemical Investment Holding Corporation | Method of preparing filters |
| WO2006071979A1 (en) | 2004-12-28 | 2006-07-06 | E.I. Dupont De Nemours And Company | Filtration media for filtering particulate material from gas streams |
| US20060137318A1 (en) | 2004-12-28 | 2006-06-29 | Lim Hyun S | Filtration media for filtering particulate material from gas streams |
| WO2006071980A1 (en) | 2004-12-28 | 2006-07-06 | E.I. Dupont De Nemours And Company | Filtration media for filtering particulate material from gas streams |
| US20060137317A1 (en) | 2004-12-28 | 2006-06-29 | Bryner Michael A | Filtration media for filtering particulate material from gas streams |
| US20080245037A1 (en) | 2005-02-04 | 2008-10-09 | Robert Rogers | Aerosol Separator; and Method |
| WO2006096180A1 (en) | 2005-03-07 | 2006-09-14 | Gore Enterprise Holdings, Inc. | Composite filter media |
| WO2006112563A2 (en) | 2005-04-20 | 2006-10-26 | Nanophil Co., Ltd. | Filter for air cleaning and its manufacturing method |
| US7244291B2 (en) | 2005-05-02 | 2007-07-17 | 3M Innovative Properties Company | Electret article having high fluorosaturation ratio |
| US7244292B2 (en) | 2005-05-02 | 2007-07-17 | 3M Innovative Properties Company | Electret article having heteroatoms and low fluorosaturation ratio |
| EP1721555A1 (en) | 2005-05-12 | 2006-11-15 | MELITTA HAUSHALTSPRODUKTE GmbH & Co. Kommanditgesellschaft | Filter bag |
| US20060277877A1 (en) | 2005-06-10 | 2006-12-14 | Lydall, Inc. | High efficiency fuel filter |
| US20060292947A1 (en) | 2005-06-24 | 2006-12-28 | Lavietes Daniel | Polyester fiber scrim and method for making same |
| US20070054579A1 (en) | 2005-07-29 | 2007-03-08 | Reemay, Inc. | Bicomponent sheet material having liquid barrier properties |
| WO2007024445A1 (en) | 2005-08-19 | 2007-03-01 | Hollingsworth & Vose Company | Hvac meltblown nanoweb filter media |
| US20070075015A1 (en) | 2005-09-30 | 2007-04-05 | Bates W D Iii | Filtration media for liquid filtration |
| WO2007041310A2 (en) | 2005-09-30 | 2007-04-12 | E. I. Du Pont De Nemours And Company | Coalescing filtration medium and process |
| US20070074628A1 (en) | 2005-09-30 | 2007-04-05 | Jones David C | Coalescing filtration medium and process |
| WO2007041311A2 (en) | 2005-09-30 | 2007-04-12 | E. I. Du Pont De Nemours And Company | Filtration media for liquid filtration |
| US20070084786A1 (en) | 2005-10-14 | 2007-04-19 | General Electric Company | Filter, filter media, and methods for making same |
| EP1775006A1 (en) | 2005-10-14 | 2007-04-18 | General Electric Company | Filter, filter media, and methods for making same |
| DE102005055607B3 (en) | 2005-11-22 | 2007-03-22 | Helsa-Automotive Gmbh & Co. Kg | Filter for room ventilation air, particularly for motor vehicles, employs self supporting synthetic fibre fleece with dimpled or corrugated surface finish |
| US20070125700A1 (en) | 2005-12-05 | 2007-06-07 | Jiang Ding | Nanoweb composite material and gelling method for preparing same |
| EP1795248A2 (en) | 2005-12-06 | 2007-06-13 | MELITTA HAUSHALTSPRODUKTE GmbH & Co. Kommanditgesellschaft | Filter material and vacuum cleaner bag |
| DE202005019004U1 (en) | 2005-12-06 | 2007-04-19 | Melitta Haushaltsprodukte Gmbh & Co. Kg | Filter material and vacuum cleaner bag |
| DE102005059214B4 (en) | 2005-12-12 | 2007-10-25 | Eurofilters N.V. | Filter bag for a vacuum cleaner |
| WO2007068408A1 (en) | 2005-12-12 | 2007-06-21 | Eurofilters N.V. | Filter bag for a vacuum cleaner and use thereof |
| WO2007068444A1 (en) | 2005-12-12 | 2007-06-21 | Eurofilters N.V. | Vacuum cleaner filter bag |
| DE102005059214A1 (en) | 2005-12-12 | 2007-06-28 | Eurofilters N.V. | Filter bag for a vacuum cleaner and its use |
| WO2007068302A1 (en) | 2005-12-13 | 2007-06-21 | Ufi Filters S.P.A. | Method for the realisation of a filtering separator comprising a nanofibre on a substrate with filtering properties |
| WO2007076015A2 (en) | 2005-12-22 | 2007-07-05 | Lydall, Inc. | Composite dual layer hepa filter |
| US20070175195A1 (en) | 2006-01-18 | 2007-08-02 | Skirius Stephen A | Tacky Allergen Trap And Filter Medium, And Method For Containing Allergens |
| US20070175192A1 (en) | 2006-02-01 | 2007-08-02 | Advanced Flow Engineering, Inc. | Pleated hybrid air filter |
| US20070180997A1 (en) | 2006-02-09 | 2007-08-09 | 3M Innovative Properties Company | Electrets and compounds useful in electrets |
| US20070190319A1 (en) | 2006-02-13 | 2007-08-16 | Donaldson Company, Inc. | Polymer blend, polymer solution composition and fibers spun from the polymer blend and filtration applications thereof |
| WO2007112443A2 (en) | 2006-03-28 | 2007-10-04 | North Carolina State University | Micro and nanofiber nonwoven spunbonded fabric |
| DE102006017553B3 (en) | 2006-04-13 | 2007-12-27 | Eurofilters N.V. | Filter bag for a vacuum cleaner |
| US20080017038A1 (en) | 2006-07-21 | 2008-01-24 | 3M Innovative Properties Company | High efficiency hvac filter |
| WO2008011450A1 (en) | 2006-07-21 | 2008-01-24 | 3M Innovative Properties Company | High efficiency hvac filter |
| WO2008016771A1 (en) | 2006-07-31 | 2008-02-07 | 3M Innovative Properties Company | Fibrous web comprising microfibers dispersed among bonded meltspun fibers |
| US20080026661A1 (en) | 2006-07-31 | 2008-01-31 | Fox Andrew R | Fibrous web comprising microfibers dispersed among bonded meltspun fibers |
| US20080060328A1 (en) | 2006-09-12 | 2008-03-13 | Bha Group, Inc. | Filter and filter media |
| US20080069991A1 (en) | 2006-09-13 | 2008-03-20 | Anil Kohli | Bag filter comprising polyphenylene sulfide and acrylic fiber |
| JP2008095266A (en) | 2006-10-12 | 2008-04-24 | Hodai Lee | Conjugate fiber filter using nano material, production equipment of conjugate fiber filter using nano material and production method of conjugate fiber filter using nano material |
| WO2008052970A1 (en) | 2006-10-31 | 2008-05-08 | Basf Se | Method for producing a multi layer fiber web from cellulose fibers |
| WO2008057397A1 (en) | 2006-11-02 | 2008-05-15 | E.I. Dupont De Nemours And Company | Fuel filter |
| US20080105626A1 (en) | 2006-11-02 | 2008-05-08 | David Charles Jones | Fuel filter |
| WO2008057431A2 (en) | 2006-11-03 | 2008-05-15 | Allasso Industries, Inc. | An improved high surface area fiber and textiles made from the same |
| US20080108265A1 (en) | 2006-11-03 | 2008-05-08 | Behnam Pourdeyhimi | High surface area fiber and textiles made from the same |
| WO2008066813A2 (en) | 2006-11-27 | 2008-06-05 | E. I. Du Pont De Nemours And Company | Durable nanoweb scrim laminates |
| US20080134652A1 (en) | 2006-11-27 | 2008-06-12 | Hyun Sung Lim | Durable nanoweb scrim laminates |
| US20090044702A1 (en) | 2007-02-22 | 2009-02-19 | Adamek Daniel E | Filter element and method |
| WO2008103821A2 (en) | 2007-02-23 | 2008-08-28 | Donaldson Company, Inc. | Formed filter element |
| US20150121823A1 (en) * | 2007-02-28 | 2015-05-07 | Hollingsworth & Vose Company | Waved filter media and elements |
| US20080202078A1 (en) | 2007-02-28 | 2008-08-28 | Hollingsworth & Vose Company | Waved filter media and elements |
| WO2008150548A2 (en) | 2007-06-07 | 2008-12-11 | E. I. Du Pont De Nemours And Company | Process for forming a laminate of a nanoweb and a substrate, and filters utilizing the laminate |
| US20080302242A1 (en) | 2007-06-07 | 2008-12-11 | Antoine Schelling | Process for forming a laminate of a nanoweb and a substrate and filters using the laminate |
| US8679217B2 (en) | 2007-09-07 | 2014-03-25 | E I Du Pont De Nemours And Company | Pleated nanoweb structures |
| US20090120868A1 (en) | 2007-09-19 | 2009-05-14 | Mann+Hummel Gmbh | Transmission Oil Filter Comprising a Melt Blown Layer at the Downstream Side |
| US20090120048A1 (en) | 2007-11-09 | 2009-05-14 | Hollingsworth & Vose Company | Meltblown Filter Medium |
| US20100000411A1 (en) | 2007-11-09 | 2010-01-07 | Hollingsworth & Vose Company | Meltblown filter medium, related applications and uses |
| US8608817B2 (en) | 2007-11-09 | 2013-12-17 | Hollingsworth & Vose Company | Meltblown filter medium |
| US8986432B2 (en) | 2007-11-09 | 2015-03-24 | Hollingsworth & Vose Company | Meltblown filter medium, related applications and uses |
| US20110147976A1 (en) | 2007-11-09 | 2011-06-23 | Hollingsworth & Vose Company | Meltblown filter medium |
| DE202007015994U1 (en) | 2007-11-14 | 2008-01-17 | Wolf Pvg Gmbh & Co. Kg | Air filter medium |
| US20100116138A1 (en) | 2008-11-07 | 2010-05-13 | Hollingsworth & Vose Company | Multi-phase filter medium |
| US20100187712A1 (en) | 2009-01-28 | 2010-07-29 | Donaldson Company, Inc. | Method and Apparatus for Forming a Fibrous Media |
| US20100187171A1 (en) | 2009-01-28 | 2010-07-29 | Donaldson Company, Inc. | Fibrous Media |
| US8950587B2 (en) | 2009-04-03 | 2015-02-10 | Hollingsworth & Vose Company | Filter media suitable for hydraulic applications |
| US20150182885A1 (en) | 2009-04-03 | 2015-07-02 | Hollingsworth & Vose Company | Filter media suitable for hydraulic applications |
| US20110147320A1 (en) * | 2009-12-22 | 2011-06-23 | Hollingsworth & Vose Company | Filter media and articles including dendrimers and/or other components |
| US8973906B2 (en) * | 2010-02-05 | 2015-03-10 | Klingenburg Gmbh | Device for conditioning an air flow |
| US20160184751A1 (en) | 2010-04-27 | 2016-06-30 | Hollingsworth & Vose Company | Filter media with a multi-layer structure |
| US9283501B2 (en) | 2010-04-27 | 2016-03-15 | Hollingsworth & Vose Company | Filter media with a multi-layer structure |
| US8679218B2 (en) * | 2010-04-27 | 2014-03-25 | Hollingsworth & Vose Company | Filter media with a multi-layer structure |
| US9289632B2 (en) | 2010-05-07 | 2016-03-22 | Japan Vilene Company, Ltd. | Electrically charged filter and mask |
| US20120152821A1 (en) | 2010-12-17 | 2012-06-21 | Hollingsworth & Vose Company | Fine fiber filter media and processes |
| US20120152824A1 (en) | 2010-12-17 | 2012-06-21 | Hollingsworth & Vose Company | Fine fiber filter media and processes |
| US20120318754A1 (en) | 2010-12-17 | 2012-12-20 | Hollingsworth & Vose Company | Fine fiber filter media and processes |
| US20160158677A1 (en) | 2010-12-17 | 2016-06-09 | Hollingsworth & Vose Company | Fine fiber filter media and processes |
| US20140214340A1 (en) * | 2011-07-15 | 2014-07-31 | Voestalpine Stahl Gmbh | Apparatus and method for detecting at least one periodically occurring defect on an object |
| US20150167249A1 (en) | 2012-07-19 | 2015-06-18 | Aahi Kasei Fibers Corporation | Multilayered structure comprising fine fiber cellulose layer |
| US20160059167A1 (en) | 2012-11-13 | 2016-03-03 | Hollingsworth & Vose Company | Pre-coalescing multi-layered filter media |
| US20140130469A1 (en) | 2012-11-13 | 2014-05-15 | Hollingsworth & Vose Company | Multi-layered filter media |
| US20140346107A1 (en) | 2013-05-24 | 2014-11-27 | Hollingsworth & Vose Company | Filter Media Including Polymer Compositions and Blends |
| US20170248334A1 (en) * | 2014-10-29 | 2017-08-31 | Merlin Technology Gmbh | Apparatus for humidifying air in an air duct |
| US20160166953A1 (en) | 2014-12-15 | 2016-06-16 | Hollingsworth & Vose Company | Filter media including fine staple fibers |
| US20160361674A1 (en) | 2014-12-15 | 2016-12-15 | Hollingsworth & Vose Company | Filter media including fine staple fibers |
| US20160175752A1 (en) | 2014-12-19 | 2016-06-23 | Hollingsworth & Vose Company | Filter media comprising a pre-filter layer |
| US20180023824A1 (en) * | 2015-02-13 | 2018-01-25 | Merlin Technology Gmbh | Long-range nozzle for entry of air |
| US20180001244A1 (en) | 2016-07-01 | 2018-01-04 | Hollingsworth & Vose Company | Multi-layered electret-containing filtration media |
| US20180236384A1 (en) | 2017-02-21 | 2018-08-23 | Hollingsworth & Vose Company | Electret-containing filter media |
| US20180236389A1 (en) | 2017-02-21 | 2018-08-23 | Hollingsworth & Vose Company | Electret-containing filter media |
| US20180236385A1 (en) | 2017-02-21 | 2018-08-23 | Hollingsworth & Vose Company | Electret-containing filter media |
| US20180243674A1 (en) | 2017-02-21 | 2018-08-30 | Hollingsworth & Vose Company | Electret-containing filter media |
| US20220381455A1 (en) * | 2021-06-01 | 2022-12-01 | Shenzhen Envicool Technology Co., Ltd. | Indirect evaporative cooling air conditioner |
Non-Patent Citations (11)
| Title |
|---|
| "Acrylic fiber" Wikipedia published Jun. 5, 2015 (Year: 2015). * |
| "Relative Permittivity—Dielectric Constant" The Engineering Toolbox published Jul. 2, 2014 accessed at <https://web.archive.org/web/20140702232754/https://www.engineeringtoolbox.com/relative-permittivity-d_1660.html> (Year: 2014). * |
| Deka et al., Gradient density media for liquid filtration. Filtration News. 2004;22(4):24, 26, 28, 30, 32 and 33. |
| International Search Report and Written Opinion for PCT/US17/40287 mailed Sep. 15, 2017. |
| International Search Report and Written Opinion for PCT/US17/43249 mailed Oct. 10, 2017. |
| Kaukopaasi et al., Multilayered sheets: the media of the future for automotive filtration applications? TAPPI Journal. 1992;75(1):127-32. |
| Kaukopaasi et al., Multi-layered sheet—the future media for automotive filtration applications? Nonwoven Conference. TAPPI Proceedings. 1991;137-154. |
| Lloyd et al., Layer mixing during three-layer stratified forming: the role of vane length and mix-wire speed difference. TAPPI Journal. Nov. 1998;81(11):194-202. |
| Montefusco et al., The use of nonwovens in air filtration. Filtration and Separation. 2005;42(2):30-1. |
| Rodman, Fibers for nonwovens with emphasis on filtration theory and applications. Book of Papers for the National Technical Conference of AATCC. Jan. 1990:233-45. |
| U.S. Appl. No. 15/200,612, filed Jul. 1, 2016, Zhu et al. |
Also Published As
| Publication number | Publication date |
|---|---|
| US20180001247A1 (en) | 2018-01-04 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US12420221B2 (en) | Multi-layered electret-containing filtration media | |
| US20180001244A1 (en) | Multi-layered electret-containing filtration media | |
| US20220126226A1 (en) | Electret-containing filter media | |
| US12220659B2 (en) | Electret-containing filter media | |
| US20220105453A1 (en) | Electret-containing filter media | |
| US11123668B2 (en) | Filter media including a filtration layer comprising synthetic fibers | |
| US20220054961A1 (en) | Electret-containing filter media | |
| CN105209147B (en) | Filter Media and Elements | |
| US7691168B2 (en) | Highly charged, charge stable nanofiber web | |
| AU2007356885B2 (en) | Highly charged, charge stable nanofiber web | |
| WO2018156561A1 (en) | Electret-containing filter media | |
| JP2024099718A (en) | Filter medium having nonwoven fabric layer and meltblown layer and gas turbine including the filter medium | |
| EP3519076A1 (en) | Filter media including flame retardant fibers | |
| WO2018017937A1 (en) | Multi-layered electret-containing filtration media | |
| JPWO2019230983A1 (en) | Filter filter media and filter unit equipped with this | |
| JP7356972B2 (en) | Filter medium and filter unit equipped with the same |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| AS | Assignment |
Owner name: HOLLINGSWORTH & VOSE COMPANY, MASSACHUSETTS Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:JINKA, SUDHEER;HEALEY, DAVID T.;GALLIMORE, MARK A.;SIGNING DATES FROM 20161229 TO 20170116;REEL/FRAME:041183/0602 |
|
| STPP | Information on status: patent application and granting procedure in general |
Free format text: FINAL REJECTION MAILED |
|
| STPP | Information on status: patent application and granting procedure in general |
Free format text: DOCKETED NEW CASE - READY FOR EXAMINATION |
|
| STPP | Information on status: patent application and granting procedure in general |
Free format text: NON FINAL ACTION MAILED |
|
| STPP | Information on status: patent application and granting procedure in general |
Free format text: RESPONSE TO NON-FINAL OFFICE ACTION ENTERED AND FORWARDED TO EXAMINER |
|
| STPP | Information on status: patent application and granting procedure in general |
Free format text: DOCKETED NEW CASE - READY FOR EXAMINATION |
|
| STPP | Information on status: patent application and granting procedure in general |
Free format text: NON FINAL ACTION MAILED |
|
| STPP | Information on status: patent application and granting procedure in general |
Free format text: RESPONSE TO NON-FINAL OFFICE ACTION ENTERED AND FORWARDED TO EXAMINER |
|
| STPP | Information on status: patent application and granting procedure in general |
Free format text: FINAL REJECTION MAILED |
|
| AS | Assignment |
Owner name: BANK OF AMERICA, N.A., AS COLLATERAL AGENT, NORTH CAROLINA Free format text: NOTICE OF GRANT OF SECURITY INTEREST IN PATENTS;ASSIGNOR:HOLLINGSWORTH & VOSE COMPANY;REEL/FRAME:058649/0109 Effective date: 20211230 |
|
| STPP | Information on status: patent application and granting procedure in general |
Free format text: DOCKETED NEW CASE - READY FOR EXAMINATION |
|
| STPP | Information on status: patent application and granting procedure in general |
Free format text: NON FINAL ACTION MAILED |
|
| STPP | Information on status: patent application and granting procedure in general |
Free format text: FINAL REJECTION MAILED |
|
| STCV | Information on status: appeal procedure |
Free format text: NOTICE OF APPEAL FILED |
|
| STPP | Information on status: patent application and granting procedure in general |
Free format text: RESPONSE TO NON-FINAL OFFICE ACTION ENTERED AND FORWARDED TO EXAMINER |
|
| STPP | Information on status: patent application and granting procedure in general |
Free format text: NON FINAL ACTION MAILED |
|
| STPP | Information on status: patent application and granting procedure in general |
Free format text: RESPONSE TO NON-FINAL OFFICE ACTION ENTERED AND FORWARDED TO EXAMINER |
|
| STPP | Information on status: patent application and granting procedure in general |
Free format text: FINAL REJECTION MAILED |
|
| STPP | Information on status: patent application and granting procedure in general |
Free format text: NOTICE OF ALLOWANCE MAILED -- APPLICATION RECEIVED IN OFFICE OF PUBLICATIONS |
|
| STPP | Information on status: patent application and granting procedure in general |
Free format text: NOTICE OF ALLOWANCE MAILED -- APPLICATION RECEIVED IN OFFICE OF PUBLICATIONS |
|
| STPP | Information on status: patent application and granting procedure in general |
Free format text: PUBLICATIONS -- ISSUE FEE PAYMENT RECEIVED |
|
| STPP | Information on status: patent application and granting procedure in general |
Free format text: PUBLICATIONS -- ISSUE FEE PAYMENT VERIFIED |
|
| STCF | Information on status: patent grant |
Free format text: PATENTED CASE |